JPS60178846A - Production of mixed quaternary ammonium salt - Google Patents

Production of mixed quaternary ammonium salt

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Publication number
JPS60178846A
JPS60178846A JP3500884A JP3500884A JPS60178846A JP S60178846 A JPS60178846 A JP S60178846A JP 3500884 A JP3500884 A JP 3500884A JP 3500884 A JP3500884 A JP 3500884A JP S60178846 A JPS60178846 A JP S60178846A
Authority
JP
Japan
Prior art keywords
tertiary amine
benzyl
chain alkyl
benzyl halide
amine
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
JP3500884A
Other languages
Japanese (ja)
Other versions
JPH0428252B2 (en
Inventor
Koichi Fujita
耕一 藤田
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.)
Mitsubishi Petrochemical Co Ltd
Original Assignee
Mitsubishi Petrochemical 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 Mitsubishi Petrochemical Co Ltd filed Critical Mitsubishi Petrochemical Co Ltd
Priority to JP3500884A priority Critical patent/JPS60178846A/en
Publication of JPS60178846A publication Critical patent/JPS60178846A/en
Publication of JPH0428252B2 publication Critical patent/JPH0428252B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To produce the titled substance useful as a disinfectant, in a short time, leaving little unreacted material, by reacting a benzyl halide first with an amine composed mainly of a branched-chain alkyl tertiary amine and then with a straight-chain alkyl tertiary amine, in the reaction of an aliphatic tertiary amine with a benzyl halide. CONSTITUTION:The objective compound is produced by reacting an aliphatic tertiary amine with a benzyl halide. In the above process, a tertiary amine composed mainly of a branched-chain alkyl tertiary amine is made to react with excess benzyl halide (benzyl chloride or benzyl brmide), and then a straight-chain alkyl tertiary amine having high reactivity is made to react with the benzyl halide at stoichiometric ratio by adding the tertiary amine in an amount corresponding to the remaining benzyl halide or if the remaining benzyl halide is little, adding necessary amount of the benzyl halide to the system. The above reaction is preferably carried out by using a solvent such as ethanol.

Description

【発明の詳細な説明】 本発明は脂肪族第3級アミンとハロゲン化ベンジルとを
反応させて、直鎖アル、キル第4級アンモニウム塩と分
岐鎖アルキル第4級アンモニウム塩の混合溶液を製造す
る方法に関するものである。
Detailed Description of the Invention The present invention involves reacting an aliphatic tertiary amine with a benzyl halide to produce a mixed solution of a linear alkyl quaternary ammonium salt and a branched alkyl quaternary ammonium salt. It's about how to do it.

脂肪族第4級ベンジルアンモニウム塩、特に脂肪族第4
級ベンジルアンモニウムクロライドは殺菌・消毒剤とし
て有用である。しかしながら、このような用途に使用さ
れる第4級アンモニウム塩は未反応アミンの含有量の少
ないことが必要である。未反応アミンの残存量を少なく
するには、通常アミンに対し過剰のハロゲン化ベンジル
を用いることによって可能であるが、」二記用途に用い
られる第4級アンモニウム塩は未反応塩化ベンジルの含
有量の少ないことも必要で、アミンに対し過剰のハロゲ
ン化ベンジルを用いた場合、反応路r後、未反応ハロゲ
ン化ベンジルを分離し精製する必要がある。
Aliphatic quaternary benzyl ammonium salts, especially aliphatic quaternary benzyl ammonium salts
Class benzyl ammonium chloride is useful as a disinfectant. However, the quaternary ammonium salt used for such applications needs to have a low content of unreacted amine. The amount of residual unreacted amine can be reduced by using an excess of benzyl halide relative to the amine. It is also necessary that the amount of benzyl halide is small, and if an excess of benzyl halide is used with respect to the amine, it is necessary to separate and purify the unreacted benzyl halide after reaction route r.

しかしながら、反応終丁後に未反応ハロゲン化ベンジル
を蒸留で除こうとすると、ハロゲン化ヘンシル類は沸点
が高いので(塩化ベンジルは179°C1臭化ベンジル
は198°C)反応溶媒として用いたエタノール、イソ
プロパツールが先に留去し、粘稠な液状となり蒸留が困
難になる。溶媒として沸点が高いエチレングリコール(
沸点197°C)、プロピレングリコール(沸点188
℃)等の2価アルコールを用いると、装置1+t:ハロ
ゲン化ヘンシルの除去蒸留の際に目的生成物の第4級ア
ンモニウム塩が高温で長時間加熱されることにより分解
するという別の問題を生ずる。従って未反応アミンと未
反応ハロゲン化ベンジル両方の残存量を少なくするには
アミンとハロゲン化ベンジルの1iEr論量を正確に反
11ト+させる必要がある。
However, when attempting to remove unreacted benzyl halide by distillation after the reaction has ended, since the boiling point of hensyl halides is high (179°C for benzyl chloride and 198°C for benzyl bromide), the ethanol used as the reaction solvent, The isopropanol is distilled off first and becomes a viscous liquid, making it difficult to distill. Ethylene glycol with a high boiling point as a solvent (
(boiling point 197°C), propylene glycol (boiling point 188°C)
When using a dihydric alcohol such as (℃), another problem arises in that the quaternary ammonium salt of the target product is decomposed by being heated at high temperature for a long time during apparatus 1+t: removal distillation of halogenated Henssil. . Therefore, in order to reduce the residual amount of both the unreacted amine and the unreacted benzyl halide, it is necessary to precisely adjust the stoichiometric amounts of 1iEr of the amine and benzyl halide to 11t+.

前記用途に用いられるアミンはボr IJr3類を出発
原料として得られる直鎖アミンを主成分とする所謂天然
アミンと、オキソ法で合成される高級アルコールをアル
キルクロリドに転換した後、これを低級ジアルキルアミ
ンでアミノ化する方法または特開昭58−105945
号明細書に開示されているように、長鎖オレフィンの低
級ジアルキルアミンとを水素、−酸化炭素混合ガスの存
在下に反応させる方法によって得られる合成アミンとに
大別できる。合成アミンは一般に分岐鎖アルキル第3級
アミンを20〜60重量%含む分岐鎖・直鎖混合アルキ
ル第3級アミンである。
The amines used for the above purpose are so-called natural amines mainly composed of linear amines obtained using Bor IJr3 as starting materials, and higher alcohols synthesized by the oxo method, which are converted into alkyl chlorides, and then converted into lower dialkyl chlorides. Amination method with amine or JP-A-58-105945
As disclosed in the specification, synthetic amines can be broadly classified into synthetic amines obtained by a method of reacting a long-chain olefin with a lower dialkylamine in the presence of a hydrogen and carbon oxide mixed gas. The synthetic amine is generally a mixed branched and linear alkyl tertiary amine containing 20 to 60% by weight of branched alkyl tertiary amine.

反応生成物中の未反応アミンと未反応ハロゲン化ベンジ
ル両方の残存量を少なくするために、直鎖アミンとハロ
ゲン化ベンジンを量論量で反応させた場合には短11o
t間に反応が進むが、分岐鎖・直鎖混合アルキル第3級
アミンを同様に反応させると分岐鎖アルキル第3級アミ
ンの反応速度が直鎖アルキル第3級アミンに比して著し
く遅く、直鎖アルギル第3級アミンの反応率が100%
に達しても、分岐鎖アルキル第3級アミンの未反応分が
多い。この反応率を高めるためにはハロゲン化ベンジル
の過刺叶の使用が必要で、その結果ハロゲン化ベンジル
残存量の低減が困難である。
In order to reduce the residual amount of both unreacted amine and unreacted benzyl halide in the reaction product, when linear amine and benzyl halide are reacted in stoichiometric amounts,
The reaction progresses during time t, but when branched and straight chain mixed alkyl tertiary amines are reacted in the same way, the reaction rate of the branched chain alkyl tertiary amine is significantly slower than that of the straight chain alkyl tertiary amine. Reaction rate of linear argyl tertiary amine is 100%
Even if this amount is reached, there is still a large amount of unreacted branched alkyl tertiary amine. In order to increase this reaction rate, it is necessary to use oversprings of benzyl halide, and as a result, it is difficult to reduce the residual amount of benzyl halide.

本発明はこのような混合アミンのハロゲン化ヘンシルに
よる4級化を、比較的短時間に完結し、か1〕、未反応
アミンと未反応ハロゲン化ベンジル残存量を少なくする
ことを可能とするもので、脂混合溶液を製造する方法に
おいて、まず分岐鎖アルキル第3級アミンを主成分とす
る第3級アミンを過剰量のハロゲン化ベンジルと反応さ
せた後、実質的に分岐鎖アルキル基を含まない直鎖アル
キル第3級アミンを加えてハロゲン化ベンジルトヲ反応
させることを特徴とする混合第4級アンモニウム塩の製
造方法である。
The present invention makes it possible to complete the quaternization of such a mixed amine with a hensyl halide in a relatively short time, and to reduce the amount of unreacted amine and unreacted benzyl halide remaining (1). In the method for producing a fat mixed solution, first, a tertiary amine containing a branched chain alkyl tertiary amine as a main component is reacted with an excess amount of benzyl halide, and then a mixture containing substantially branched chain alkyl groups is reacted. This is a method for producing a mixed quaternary ammonium salt, which is characterized by adding a straight chain alkyl tertiary amine and reacting the halogenated benzyl amine.

本発明で原料として用いられる長鎖アルキル第3級アミ
ンのうち直鎖アルキルアミンは一般式(但し R1およ
びR2はそれぞれ独立にメチル基またはエチル基であり
、R3は炭素数が8〜25の直鎖アルキル基である。)
で示される脂肪族第3級アミンであり、また分岐鎖アル
キルアミンは一般(但し、R1およびR2はそれぞれ独
立にメチルノ1(またはエチル基であり、R4およびR
5はそれぞれ直鎖アルキル基であり、R4とR5の炭素
数の合計が6〜23である。)で示される脂肪族第3級
アミンである。
Among the long-chain alkyl tertiary amines used as raw materials in the present invention, the straight-chain alkyl amine has the general formula (wherein R1 and R2 are each independently a methyl group or an ethyl group, and R3 is a straight chain having 8 to 25 carbon atoms). (It is a chain alkyl group.)
It is an aliphatic tertiary amine represented by
5 is a linear alkyl group, and the total number of carbon atoms in R4 and R5 is 6 to 23. ) is an aliphatic tertiary amine represented by

本発明の方法においては、まず分岐鎖アルキル第3級ア
ミンを主成分とする第3級アミンを過剰litのハロゲ
ン化ベンジルにより4級化し、次いで反応性の高い直鎖
アルキル第3級アミンをハロゲン化ベンジルの残存量に
見合った量だけ加えるか、または加えるべき直鎖アルキ
ル第3級アミン量よ11Jモハロゲン化ベンジルの残存
量が少ない場合には更に必要量のノ・ロゲン化ベンジル
を加えて、直鎖アルキル第3級アミンとハロゲン化ベン
ジルをjft m 15にで反応させることにより、短
い時間で未反応アミンと未反応ノーロゲン化ベンジルの
残存量の少ない混合アルキル第4級アンモニウム塩を得
ることができる。
In the method of the present invention, a tertiary amine whose main component is a branched alkyl tertiary amine is first quaternized with excess lit of benzyl halide, and then a highly reactive straight chain alkyl tertiary amine is converted into a halogenated tertiary amine. Add an amount commensurate with the remaining amount of benzyl chloride, or if the remaining amount of 11J mohalogenated benzyl is smaller than the amount of linear alkyl tertiary amine to be added, add the necessary amount of benzyl halogenide, By reacting a linear alkyl tertiary amine and a halogenated benzyl at jft m 15, it is possible to obtain a mixed alkyl quaternary ammonium salt in a short time with a small amount of unreacted amine and unreacted benzyl halogenide remaining. can.

本発明の方法における第3級アミンとノ・ロゲン化ヘン
シルとの反応は公知の如くエタノール、イソプロパツー
ル、エチレングリコール、ブロヒ゛レンゲリコール等の
1価または2価の低級アルコール溶媒中で行なうことに
より、反応液の粘度上昇による反応速度の低下を防ぐこ
とができる。更に反応速度を速くするためにアルカリ剤
または水を加えることができる。アルカリ剤は木酢化ナ
トリウム、水酸化カリ、炭酸ナトリウム、重炭酸ナトリ
ウムなどが用いられる。
In the method of the present invention, the reaction between the tertiary amine and the halogenated hensyl is carried out in a monohydric or dihydric lower alcohol solvent such as ethanol, isopropanol, ethylene glycol, or brohylene gelicol, as is known in the art. This can prevent a decrease in the reaction rate due to an increase in the viscosity of the reaction solution. Furthermore, an alkaline agent or water can be added to speed up the reaction rate. As the alkaline agent, sodium pyrolyl acetate, potassium hydroxide, sodium carbonate, sodium bicarbonate, etc. are used.

反応温度は40〜120°Cの範囲内で選択することが
でき、反応圧力は大気圧下でもよいが、反応溶媒の種類
と反応温度によっては加圧状態に保ってもよい。
The reaction temperature can be selected within the range of 40 to 120°C, and the reaction pressure may be at atmospheric pressure, but may be maintained under pressure depending on the type of reaction solvent and reaction temperature.

本発明における原料の第3級アミンとしては、例えばオ
キソ法により合成された分岐鎖、直鎖混合アルキル第3
級アミンを用いることができる。
The tertiary amine as a raw material in the present invention includes, for example, branched and linear mixed alkyl tertiary amines synthesized by the oxo method.
grade amines can be used.

この場合には、分岐鎖アルキル第3級アミンと直鎖アル
キル第3級アミンとは沸点が異なるので、蒸留により両
者を分別する。この分別蒸留においては、分岐鎖アルキ
ル第3級アミン量分中には直鎖アルキル第3級アミンは
15〜30重111%、場合によってはそれ以上の混入
が許されるが、直鎖アルキル第3級アミン量分中の分岐
鎖アルキル第3級アミンの混入量は1重量%以下である
ことが好ましい。
In this case, since the branched chain alkyl tertiary amine and the straight chain alkyl tertiary amine have different boiling points, they are separated by distillation. In this fractional distillation, linear alkyl tertiary amines are allowed to be mixed in an amount of 15 to 30% by weight, or even more in some cases, in the amount of branched alkyl tertiary amines. The amount of branched chain alkyl tertiary amine mixed in the amount of primary amine is preferably 1% by weight or less.

ハロゲン化ベンジルとしては塩化ベンジル、臭化ベンジ
ルが用いられる。
As the benzyl halide, benzyl chloride and benzyl bromide are used.

以下、実施例および比較例により本発明を具体的に説明
するが、本発明はこれらの実施例により限定されるもの
ではない。
EXAMPLES Hereinafter, the present invention will be specifically explained with reference to Examples and Comparative Examples, but the present invention is not limited to these Examples.

参考例(直鎖アルキル第3級アミンの4級化反応)試薬
N、N−ジメヂルドデシルアミンを蒸留し不純物を除い
たもの213,4 g (1,0モル)とインプロパツ
ール213.4 g 、水5.5gをガラス製反応槽に
仕込み、攪拌しながら加熱し60°Cに保ち、塩化ベン
ジル126.6 g (1,0モル)を1時間で滴下し
た。滴下終了後60’Cで4時間反応を続行した。
Reference example (quaternization reaction of linear alkyl tertiary amine) 213.4 g (1.0 mol) of reagent N,N-dimedyldodecylamine distilled to remove impurities and Impropatol 213.4 A glass reaction tank was charged with 5.5 g of water, heated with stirring and maintained at 60°C, and 126.6 g (1.0 mol) of benzyl chloride was added dropwise over 1 hour. After the dropwise addition was completed, the reaction was continued at 60'C for 4 hours.

Jy−比法の一部を採取し、n−ヘキサン/メタノール
/水混合液を加えることにより、未反応アミンと未反応
塩化ベンジルをn−ヘキサン相に抽出し、n−ヘキサン
相をガスクロ分析する方法により未反応アミンと未反応
塩化ベンジル濃度を測定した。
Collect a portion of the Jy-ratio and add a mixture of n-hexane/methanol/water to extract unreacted amine and unreacted benzyl chloride into the n-hexane phase, and analyze the n-hexane phase by gas chromatography. The unreacted amine and unreacted benzyl chloride concentrations were determined by the method.

未反応アミン濃度は0.22重量%(アミン反応率99
.4モル%)、未反応塩化ベンジル濃度はJ1重lit
%であった。
The unreacted amine concentration was 0.22% by weight (amine reaction rate 99%).
.. 4 mol%), unreacted benzyl chloride concentration is J1 heavy lit
%Met.

比較例(分岐鎖と直鎖アルキル混合第3級アミンの4級
化反応) 1−ドデセンとジメチルアミンおよび水素°−酸化炭素
混合ガスより合成したN、N−ジメチル−トリデシルア
ミン227.4 g (1,0モル)直鎖率61.4重
量%)とインプロパツール227.4 g 。
Comparative Example (Quaternization reaction of branched and linear alkyl mixed tertiary amine) 227.4 g of N,N-dimethyl-tridecylamine synthesized from a mixed gas of 1-dodecene, dimethylamine, and hydrogen °-carbon oxide (1.0 mol) linearity 61.4% by weight) and Improper Tool 227.4 g.

水6gをガラス製反応槽に仕込み、攪拌しながら加熱し
60°Cに保ち、all化ヘンシルl 39,3 g 
(1,1モル)を1時間で滴下した。滴下終了後60°
Cで8時間反応を続行した。未反応アミン濃度(直鎖ア
ミン」−分岐鎖アミン)は0.5重1fk% (アミン
反応率98.7モル%)、未反応塩化ベンジル濃度は2
.4重量%であった。
Pour 6 g of water into a glass reaction tank, heat it while stirring and keep it at 60°C, and add 39.3 g of allied Henssil l.
(1.1 mol) was added dropwise over 1 hour. 60° after completion of dripping
The reaction was continued for 8 hours at C. The unreacted amine concentration (linear amine - branched chain amine) was 0.5 Fk% (amine reaction rate 98.7 mol%), and the unreacted benzyl chloride concentration was 2.
.. It was 4% by weight.

この間の直鎖アルキル第3級アミンと分岐鎖アルキル第
3級アミンの反応率の変化を第1表に示す。直鎖アルキ
ル第3級アミンに比し、分岐鎖アルキル第3級アミンの
反応速度が極めて遅いことがわかる。
Table 1 shows the change in the reaction rate between the linear alkyl tertiary amine and the branched alkyl tertiary amine during this period. It can be seen that the reaction rate of branched chain alkyl tertiary amines is extremely slow compared to that of straight chain alkyl tertiary amines.

実施例(分岐鎖アルキル第3級アミンと直鎖アルキル第
3級アミンの分別4級化反応) 1−ドデセンとジメチルアミンおよび水素・−酸化炭素
混合ガスより合成したN、N−ジメチル−トリデシルア
ミンを、内径4 c1n%理論段数20段の蒸留塔を用
いて210 mm Hgの圧力で蒸留し、沸点137.
5〜146.5℃の分岐鎖アミンを主成分とする留分1
と、沸点14 J5°Cの実質的に直鎖アミンからなる
留分2に分けた。留分1は直鎖アミン25重量%と分岐
鎖アミン75重量%がらなり、留分2は直鎖アミンが9
9.5重量%で分岐鎖アミンは0.5重量%であった。
Example (Fractional quaternization reaction of branched-chain alkyl tertiary amine and straight-chain alkyl tertiary amine) N,N-dimethyl-tridecyl synthesized from 1-dodecene, dimethylamine, and hydrogen/carbon oxide mixed gas The amine was distilled at a pressure of 210 mm Hg using a distillation column with an internal diameter of 4 c1n% and 20 theoretical plates, and the boiling point was 137.
Fraction 1 mainly composed of branched chain amines at 5 to 146.5°C
and fraction 2 consisting essentially of linear amines with a boiling point of 14°C. Fraction 1 consists of 25% by weight of linear amines and 75% by weight of branched amines, and fraction 2 consists of 9% by weight of linear amines.
9.5% by weight and branched amine was 0.5% by weight.

留分lを153g(o、67モル)とイソプロパツール
153gおよび水3.4gをガラス製反応槽に仕込み、
攪拌しながら加熱し60°Cに保ち、塩化ベンジル18
9.9 g (1,5モル)を15分間で滴下した。滴
下終了後60°Cで4時間反応を続行した。直鎖アミン
の反応率は100モル%で、分岐鎖アミンの反応率は9
9.7モル%であった。未反応塩化ベンジル残存濃度は
21.0重量%であった。
153 g (o, 67 mol) of fraction 1, 153 g of isopropanol, and 3.4 g of water were charged into a glass reaction tank.
Heat with stirring and maintain at 60°C, and add benzyl chloride 18
9.9 g (1.5 mol) were added dropwise over 15 minutes. After the dropwise addition was completed, the reaction was continued at 60°C for 4 hours. The reaction rate of linear amine is 100 mol%, and the reaction rate of branched chain amine is 9
It was 9.7 mol%. The residual concentration of unreacted benzyl chloride was 21.0% by weight.

次いで前記留分2の直鎖アミン188 g (0,83
モル)とイソプロパツール188gおよび水3.8gを
加え60°Cで第2段目の反応を4時間行なった。第1
段と第2段の反応で加えた全アミンの未反応残存濃度は
0.13重IIじ (アミン反応率99.5モル%)で
未反応塩化ベンジル残存濃度はJl爪量%以下であった
Next, 188 g (0,83
mol), 188 g of isopropanol, and 3.8 g of water were added, and a second stage reaction was carried out at 60°C for 4 hours. 1st
The unreacted residual concentration of all the amines added in the reactions of stage and second stage was 0.13 times II (amine reaction rate 99.5 mol%), and the residual concentration of unreacted benzyl chloride was less than Jl mass %. .

第1表 出願人 三菱油化株式会社 代理人 弁理士厚田桂一部Table 1 Applicant: Mitsubishi Yuka Co., Ltd. Agent: Patent attorney Katsura Atsuta

Claims (4)

【特許請求の範囲】[Claims] (1) 脂肪に第3級アミンとハロゲン化ベンジルとを
反応させて、直鎖アルキル第4級アンモニウム塩と分岐
鎖アルキール第4級アンモニウム塩との混合溶液を製造
する方法において、まず分岐鎖アルキル第3級アミンを
主成分とする第3級アミンを過剰量のハロゲン化ベンジ
ルと反応させた後、実質的に分岐鎖アルキル基を含まな
い直鎖アルキル第3級アミンを加えてハロゲン化ベンジ
ルと反応させることを特徴とする混合第4級アンモニウ
ム塩の製造方法。
(1) In a method for producing a mixed solution of a straight-chain alkyl quaternary ammonium salt and a branched-chain alkyl quaternary ammonium salt by reacting a tertiary amine and a benzyl halide with a fat, first, a branched-chain alkyl quaternary ammonium salt is produced. After reacting a tertiary amine whose main component is a tertiary amine with an excess amount of benzyl halide, a linear alkyl tertiary amine containing substantially no branched chain alkyl group is added to react the benzyl halide. A method for producing a mixed quaternary ammonium salt, the method comprising reacting the mixed quaternary ammonium salt.
(2)直鎖アルキル第3級アミンが一般式%式% (1但し、R1およびR2はそれぞれ独立にメチル基ま
たけエチル基であり、R3は炭素数が8〜25の直鎖ア
ルキル基である。)で示される脂肪族第3級アミンであ
る、特許請求の範囲第(1)項に記載の方法。
(2) Straight-chain alkyl tertiary amine has the general formula % (1) However, R1 and R2 are each independently a methyl group or ethyl group, and R3 is a straight-chain alkyl group having 8 to 25 carbon atoms. The method according to claim (1), wherein the aliphatic tertiary amine is an aliphatic tertiary amine represented by:
(3) 分岐mアルキル第3級アミンが一般式(但し、
R1およびR2はそれぞれ独立にメチル基またはエチル
基であり、R4およびR5はそれぞれ直鎖アルキル基で
あり、R4とR5の炭素数の合計が6〜23である。)
で示される脂肪族第3級アミンである、特許請求の範囲
第(1)項または第(2)項に記載の方法。
(3) The branched m-alkyl tertiary amine has the general formula (however,
R1 and R2 are each independently a methyl group or an ethyl group, R4 and R5 are each a linear alkyl group, and the total number of carbon atoms in R4 and R5 is 6 to 23. )
The method according to claim (1) or (2), wherein the aliphatic tertiary amine is an aliphatic tertiary amine represented by:
(4) ハロゲン化ベンジルが塩化ベンジルまたは臭化
ベンジルである、特許請求の範囲第(1)項から第(3
)項のいずれかに記載の方法。
(4) Claims (1) to (3) wherein the benzyl halide is benzyl chloride or benzyl bromide.
) The method described in any of the above.
JP3500884A 1984-02-25 1984-02-25 Production of mixed quaternary ammonium salt Granted JPS60178846A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3500884A JPS60178846A (en) 1984-02-25 1984-02-25 Production of mixed quaternary ammonium salt

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3500884A JPS60178846A (en) 1984-02-25 1984-02-25 Production of mixed quaternary ammonium salt

Publications (2)

Publication Number Publication Date
JPS60178846A true JPS60178846A (en) 1985-09-12
JPH0428252B2 JPH0428252B2 (en) 1992-05-13

Family

ID=12430055

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3500884A Granted JPS60178846A (en) 1984-02-25 1984-02-25 Production of mixed quaternary ammonium salt

Country Status (1)

Country Link
JP (1) JPS60178846A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5349106A (en) * 1990-08-18 1994-09-20 Henkel Kommanditgesellschaft Auf Aktien Process for reducing the residual content of free alkylating agent in aqueous solutions of cationic surfactants

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5349106A (en) * 1990-08-18 1994-09-20 Henkel Kommanditgesellschaft Auf Aktien Process for reducing the residual content of free alkylating agent in aqueous solutions of cationic surfactants

Also Published As

Publication number Publication date
JPH0428252B2 (en) 1992-05-13

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