JPS6318936B2 - - Google Patents

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Publication number
JPS6318936B2
JPS6318936B2 JP56012124A JP1212481A JPS6318936B2 JP S6318936 B2 JPS6318936 B2 JP S6318936B2 JP 56012124 A JP56012124 A JP 56012124A JP 1212481 A JP1212481 A JP 1212481A JP S6318936 B2 JPS6318936 B2 JP S6318936B2
Authority
JP
Japan
Prior art keywords
reaction
group
carbon atoms
polymerization
quaternary ammonium
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
Application number
JP56012124A
Other languages
Japanese (ja)
Other versions
JPS57126452A (en
Inventor
Akira Okada
Kimihiko Noda
Yoichi Hasegawa
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.)
Sanyo Chemical Industries Ltd
Original Assignee
Sanyo Chemical Industries 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 Sanyo Chemical Industries Ltd filed Critical Sanyo Chemical Industries Ltd
Priority to JP1212481A priority Critical patent/JPS57126452A/en
Publication of JPS57126452A publication Critical patent/JPS57126452A/en
Publication of JPS6318936B2 publication Critical patent/JPS6318936B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は第四級アンモニウム塩の製造法に関す
るものである。さらに詳しくは第四級アンモニウ
ム基を有するビニルモノマーの製造法に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing quaternary ammonium salts. More specifically, the present invention relates to a method for producing a vinyl monomer having a quaternary ammonium group.

第四級アンモニウム塩を有するビニルモノマー
は単独重含、他のモノマーとの共重合または他の
基材へのグラフト重合などによつて陽イオン性、
導電性、水溶性、接着性などの機能をもつポリマ
ーを容易に与えるため、多くの分野で使用されて
いる。
Vinyl monomers containing quaternary ammonium salts can be made cationic by monopolymerization, copolymerization with other monomers, or graft polymerization onto other base materials.
It is used in many fields because it easily provides polymers with functions such as conductivity, water solubility, and adhesive properties.

第四級アンモニウム基を有するビニルモノマー
は通常は第三級アミノ基を有するビニルモノマー
を四級化剤と反応させて得られる。第三級アミン
の四級化剤との反応はメンシユトキン反応と通称
され、通常は第三級アミンの水溶液に四級化剤を
添加して反応が行なわれる。
Vinyl monomers having quaternary ammonium groups are usually obtained by reacting vinyl monomers having tertiary amino groups with a quaternizing agent. The reaction of a tertiary amine with a quaternizing agent is commonly called the Menshutkin reaction, and the reaction is usually carried out by adding the quaternizing agent to an aqueous solution of the tertiary amine.

しかしながら後述するような一般式(1)で示され
る第三級アミノ基含有不飽和酸エステルや不飽和
酸アミドの場合、該ビニルモノマーのエステル基
またはアミド基が極めて加水分解を受け易いため
反応中に相当する不飽和酸(アクリル酸またはメ
タクリル酸)が多量副生する結果を招くことが多
かつた。この様な不飽和酸は四級化物の品質の著
しい低下を招くのみならず第三級アミノ基含有ビ
ニルモノマーおよびその第四級アンモニウム塩の
重合を促進する傾向があり、四級化反応中に予期
せざる重合を惹起する原因となることが多かつ
た。
However, in the case of unsaturated acid esters or unsaturated acid amides containing a tertiary amino group represented by the general formula (1) as described later, the ester group or amide group of the vinyl monomer is extremely susceptible to hydrolysis, so that during the reaction This often resulted in large amounts of unsaturated acids (acrylic acid or methacrylic acid) being produced as by-products. Such unsaturated acids not only cause a significant deterioration in the quality of the quaternized product, but also tend to promote the polymerization of the tertiary amino group-containing vinyl monomer and its quaternary ammonium salt, and may cause problems during the quaternization reaction. This often caused unexpected polymerization.

この様な問題点を解決するため従来から行われ
ている方策の一つは、室温以下の低温で四級化反
応を行うことである。しかしこの場合には加水分
解速度自体は大巾に低下するが同時に四級化反応
速度も著しく低下するため、反応終了までに極め
て長時間を要し、工業的には好適な方法とは言え
なかつた。
One of the measures conventionally used to solve such problems is to carry out the quaternization reaction at a low temperature below room temperature. However, in this case, the hydrolysis rate itself is greatly reduced, but at the same time, the quaternization reaction rate is also significantly reduced, so it takes an extremely long time to complete the reaction, and it is not an industrially suitable method. Ta.

本発明者らはこの様な現状に鑑み一般式(1)で示
される第三級ビニルモノマーの四級化方法を鋭意
研究した結果、高品質の四級化物を迅速に且つ反
応中の重合トラブルなく得る方法を見出し本発明
に到つた。すなわち本発明は一般式 (式中R1はHまたはCH3;R2,R3はそれぞれ
独立に炭素数1〜4のアルキル基、または炭素数
2〜4のヒドロキシアルキル基;AはO(酸素原
子)またはNH、Bは炭素数1〜4のアルキレン
基または炭素数2〜4のヒドロキシアルキレン基
である。)で示される第三級アミノ基を有するビ
ニルモノマーを四級化剤と反応させて該モノマー
の第四級アンモニウム塩を製造する方法におい
て、反応と並行して水を断続的または連続的に添
加しながら反応を行うことを特徴とする第四級ア
ンモニウム塩の製造法である。
In view of the current situation, the present inventors have conducted intensive research on a method for quaternizing the tertiary vinyl monomer represented by the general formula (1), and have found that they can rapidly produce high-quality quaternized products and eliminate polymerization problems during the reaction. The present invention was achieved by finding a method to obtain the above-mentioned results. That is, the present invention is based on the general formula (In the formula, R 1 is H or CH 3 ; R 2 and R 3 are each independently an alkyl group having 1 to 4 carbon atoms, or a hydroxyalkyl group having 2 to 4 carbon atoms; A is O (oxygen atom) or NH, B is an alkylene group having 1 to 4 carbon atoms or a hydroxyalkylene group having 2 to 4 carbon atoms.) A vinyl monomer having a tertiary amino group represented by This is a method for producing a quaternary ammonium salt, which is characterized in that the reaction is carried out while adding water intermittently or continuously in parallel with the reaction.

一般式(1)において、R2,R3はそれぞれ炭素数
1〜4のアルキル基または炭素数2〜4のヒドロ
キシアルキル基である。炭素数1〜4のアルキル
基としては、メチル基、エチル基、n−もしくは
iso−プロピル基、およびブチル基をあげること
ができる。炭素数2〜4のヒドロキシアルキル基
としては−CH2CH2OH,−CH2CH2CH2OHおよ
び−CH2CH(CH2OH)CH3をあげることができ
る。Bは炭素数1〜4のアルキレン基または炭素
数2〜4のヒドロキシアルキレン基である。該ア
ルキレン基としては−CH2CH2−,−
CH2CH2CH2−,−CH2CHCH3−があげられ、該
ヒドロキシアルキレン基としては−CH2CH
(OH)CH2−があげられる。
In general formula (1), R 2 and R 3 are each an alkyl group having 1 to 4 carbon atoms or a hydroxyalkyl group having 2 to 4 carbon atoms. As the alkyl group having 1 to 4 carbon atoms, methyl group, ethyl group, n- or
Examples include iso-propyl group and butyl group. Examples of the hydroxyalkyl group having 2 to 4 carbon atoms include -CH2CH2OH , -CH2CH2CH2OH and -CH2CH ( CH2OH ) CH3 . B is an alkylene group having 1 to 4 carbon atoms or a hydroxyalkylene group having 2 to 4 carbon atoms. The alkylene group is -CH 2 CH 2 -, -
CH 2 CH 2 CH 2 −, −CH 2 CHCH 3 − are mentioned, and the hydroxyalkylene group is −CH 2 CH
(OH) CH2- is mentioned.

一般式(1)で示されるモノマーとしては具体的に
は下記のモノマーがあげられる。
Specific examples of the monomer represented by the general formula (1) include the following monomers.

(A) 第三級アミノ基含有(メタ)アクリレート (a) ジアルキルアミノアルキル(メタ)アクリ
レート ジメチルアミノエチル(メタ)アクリレー
ト、ジエチルアミノエチル(メタ)アクリレ
ートなど (b) ジアキルアミノヒドロキシアルキル(メ
タ)アクリレート ジメチルアミノ−2−ヒドロキシプロピル
(メタ)アクリレート、ジエチルアミノ−2
−ヒドロキシプロピル(メタ)アクリレート
など 上記および以下において(メタ)アクリレート
とはアクリレートおよび/またはメタアクリレー
トという。
(A) Tertiary amino group-containing (meth)acrylates (a) Dialkylaminoalkyl (meth)acrylates Dimethylaminoethyl (meth)acrylate, diethylaminoethyl (meth)acrylate, etc. (b) Diacylaminohydroxyalkyl (meth)acrylates Dimethylamino-2-hydroxypropyl (meth)acrylate, diethylamino-2
-Hydroxypropyl (meth)acrylate, etc. In the above and below, (meth)acrylate is referred to as acrylate and/or methacrylate.

(B) 第三級アミノ基含有(メタ)アクリルアミド (a) ジアルキルアミノアルキル(メタ)アクリ
ルアミド ジメチルアミノエチル(メタ)アクリルア
ミド、ジエチルアミノプロピル(メタ)アク
リルアミドなど (b) ジアルキルアミノヒドロキミアルキル(メ
タ)アクリルアミド ジメチルアミノ−2−ヒドロキシプロピル
(メタ)アクリルアミド、ジエチルアミノ−
2−ヒドロキシプロピル(メタ)アクリルア
ミドなど 上記および以下において(メタ)アクリルアミ
ドとはアクリルアミドおよび/またはメタアクリ
ルアミドをいう。
(B) Tertiary amino group-containing (meth)acrylamides (a) Dialkylaminoalkyl (meth)acrylamide Dimethylaminoethyl (meth)acrylamide, diethylaminopropyl (meth)acrylamide, etc. (b) Dialkylaminohydroxyalkyl (meth)acrylamide Dimethylamino-2-hydroxypropyl (meth)acrylamide, diethylamino-
2-Hydroxypropyl (meth)acrylamide, etc. In the above and below, (meth)acrylamide refers to acrylamide and/or methacrylamide.

本発明は、これらのモノマー中で四級化剤によ
る副反応(加水分解、重合など)がもつともおこ
り易い第三級アミノ基含有(メタ)アクリレート
の場合にとくに有効であり好ましい。
The present invention is particularly effective and preferred in the case of tertiary amino group-containing (meth)acrylates, which are susceptible to side reactions (hydrolysis, polymerization, etc.) due to quaternizing agents among these monomers.

本発明における四級化剤は公知のものを選ぶこ
とができ、たとえばアルキルハライド(メチルク
ロライド、メチルアイオダイド、ブチルクロライ
ド、オクチルブロマイド、ラウリルブロマイド、
ステアリルアイオダイドなど)、アラルキルハラ
イド(ベンジルクロライド、P−メチルベンジル
クロライド、P−オクチルベンジルクロライド、
フエネチルブロマイドなど)、アルキル硫酸(ジ
メチル硫酸、ジエチル硫酸など)、およびスルホ
ン酸エステル(P−トルエンスルホン酸メチルな
ど)があげられる。これらの中で工業的観点から
メチルクロライド、ベンジルクロライドおよびジ
メチル硫酸が好ましい。
The quaternizing agent used in the present invention can be selected from known ones, such as alkyl halides (methyl chloride, methyl iodide, butyl chloride, octyl bromide, lauryl bromide,
stearyl iodide, etc.), aralkyl halides (benzyl chloride, P-methylbenzyl chloride, P-octylbenzyl chloride,
phenethyl bromide, etc.), alkyl sulfates (dimethyl sulfate, diethyl sulfate, etc.), and sulfonic acid esters (methyl P-toluenesulfonate, etc.). Among these, methyl chloride, benzyl chloride and dimethyl sulfate are preferred from an industrial standpoint.

本発明における四級化反応は、反応と並行して
水を断続的または連続的にモノマーに添加しなが
ら行う。四級化反応にさいし、四級化剤は反応開
始前に反応槽内の第三級アミノ基を有するビニル
モノマーに加えておいてもよく、反応と並行して
添加していつてもよいが、反応の暴走を防ぐため
反応と並行して添加する方法が好ましい。
The quaternization reaction in the present invention is carried out while adding water intermittently or continuously to the monomer in parallel with the reaction. In the quaternization reaction, the quaternization agent may be added to the vinyl monomer having a tertiary amino group in the reaction tank before the start of the reaction, or may be added in parallel with the reaction. In order to prevent the reaction from running out of control, it is preferable to add it in parallel with the reaction.

四級化剤を反応と並行して添加する方法をとる
場合、四級化剤と水とは並行して加えてもよく、
交互に加えてもよい。またそれぞれを連続的に加
えてもよく、断続的に加えてもよい。添加の方法
はとくに限定なく常圧で滴下する方法、加圧下に
圧入する(吹込む)方法などがあげられる。
When using a method of adding the quaternizing agent in parallel with the reaction, the quaternizing agent and water may be added in parallel,
They may be added alternately. Moreover, each may be added continuously or intermittently. The method of addition is not particularly limited, and examples include a method of dropping it under normal pressure and a method of injecting it under pressure (blowing).

その他の四級化反応の条件は公知の範囲でとく
に限定なく選び得るが、以下の条件は本特許にと
くに有効でありこれらの条件で実施することが好
ましい。すなわち四級化温度は10〜60℃が好まし
く20〜40℃がさらに好ましい。四級化剤の使用量
は三級アミンモノマーのアミノ基1モルに対して
1.00〜1.20モルが好ましく、1.01〜1.10モルがさ
らに好ましい。水の量は一般式(1)で示される第三
級アミノ基を有するビニルモノマーの第四級アン
モニウム塩(四級塩モノマー)の濃度に関係し、
四級化反応終了時の四級塩モノマーの濃度は四級
化時の加水分解を押えるためできるだけ高い方が
好ましいが、高すぎると四級化反応速度が遅くな
ること、四級化中の重合が起り易くなること等の
理由で通常は50〜90重量%、好ましくは70〜85重
量%である。
Although other conditions for the quaternization reaction can be selected without particular limitation within a known range, the following conditions are particularly effective for this patent, and it is preferable to carry out the reaction under these conditions. That is, the quaternization temperature is preferably 10 to 60°C, more preferably 20 to 40°C. The amount of quaternizing agent used is per mole of amino group of tertiary amine monomer.
1.00 to 1.20 mol is preferable, and 1.01 to 1.10 mol is more preferable. The amount of water is related to the concentration of the quaternary ammonium salt (quaternary salt monomer) of the vinyl monomer having a tertiary amino group represented by the general formula (1),
The concentration of the quaternary salt monomer at the end of the quaternization reaction is preferably as high as possible in order to suppress hydrolysis during quaternization, but if it is too high, the quaternization reaction rate will be slow and polymerization during quaternization will be reduced. The content is usually 50 to 90% by weight, preferably 70 to 85% by weight, for the reason that this tends to occur.

また、四級化剤を反応と並行して添加する場合
はその添加速度は一般に系中の未反応四級化剤量
が未反応モノマーおよびこれから生成する四級塩
モノマーの合計モル数に対して通常20モル%以
下、好ましくは10モル%以下にするのが好まし
い。
In addition, when adding a quaternizing agent in parallel with the reaction, the rate of addition is generally determined based on the amount of unreacted quaternizing agent in the system relative to the total number of moles of unreacted monomers and quaternary salt monomers to be produced. It is usually 20 mol% or less, preferably 10 mol% or less.

本発明によつて得られる四級塩モノマーは反応
終了時点では四級塩の水溶液となつているがこの
ものを必要に応じてさらに希釈または濃縮しても
よい。また四級塩モノマー水溶液は必要に応じて
更にイオン交換樹脂や活性炭による処理、溶剤抽
出等により精製することができる。さらにハイド
ロキノンモノメチルエーテル、ターシヤリブチル
カテコール、ニトロソベンゼン、バラフエニレン
ジアミン、フエノチアジン、ジエチルヒドロキシ
ルアミンなど公知の重合禁止剤、EDTA、ポリ
リン酸、ニトリロトリ酢酸などの公知のキレート
剤、およびPH調整剤などの添加剤を四級化反応前
または反応後加えてもよい。
The quaternary salt monomer obtained by the present invention is an aqueous solution of the quaternary salt at the end of the reaction, but this solution may be further diluted or concentrated as necessary. Further, the quaternary salt monomer aqueous solution can be further purified by treatment with an ion exchange resin or activated carbon, solvent extraction, etc., if necessary. In addition, known polymerization inhibitors such as hydroquinone monomethyl ether, tertiary butylcatechol, nitrosobenzene, paraphenyl diamine, phenothiazine, and diethylhydroxylamine, known chelating agents such as EDTA, polyphosphoric acid, and nitrilotriacetic acid, and PH regulators, etc. Additives may be added before or after the quaternization reaction.

本発明の第四級アンモニウム塩ビニルモノマー
は単独でまたはこの第四級アンモニウム塩ビニル
モノマ以外の他のビニルモノマーとともに公知の
(共)重合方法によつて(共)重合体にすること
ができる。(共)重合体を製造する際使用できる
第四級アンモニウム塩以外の他のビニルモノマー
としては、特開昭54−102388号公報に記載の単量
体たとえば親水性の非イオン性ビニル単量体、親
水性の他のカチオン性ビニル単量体、親水性のア
ニオン性ビニル単量体および油溶性のビニル単量
体があげられる。
The quaternary ammonium salt vinyl monomer of the present invention can be made into a (co)polymer alone or together with other vinyl monomers other than the quaternary ammonium salt vinyl monomer by a known (co)polymerization method. Other vinyl monomers other than the quaternary ammonium salt that can be used in producing the (co)polymer include the monomers described in JP-A-54-102388, such as hydrophilic nonionic vinyl monomers. , other hydrophilic cationic vinyl monomers, hydrophilic anionic vinyl monomers, and oil-soluble vinyl monomers.

本発明により安定化されたモノマーは通常の方
法により重合可能である。たとえばラジカル重合
開始剤、紫外線、放射線などを使用する方法で行
うことができる。これらのうち水溶性の過硫酸塩
(過硫酸ナトリウム、過硫酸アンモニウムなど)、
アゾ化合物(アゾビスイソブチロニトリル、アゾ
ビスジメチルワレロニトリルなど)などのラジカ
ル重合開始剤を用いる方法が好ましい。
The monomers stabilized according to the invention can be polymerized by conventional methods. For example, it can be carried out by a method using a radical polymerization initiator, ultraviolet rays, radiation, or the like. Among these, water-soluble persulfates (sodium persulfate, ammonium persulfate, etc.),
A method using a radical polymerization initiator such as an azo compound (azobisisobutyronitrile, azobisdimethylvaleronitrile, etc.) is preferred.

また重合は公知の方法、たとえば水溶液重合、
乳化重合、懸濁重合、沈澱重合などの方法により
行うことができる。水溶液重合の場合にはたとえ
ば単量体を水溶液(単量体濃度はたとえば10〜90
重量%)とし、系内を不活性ガスで置換したの
ち、ラジカル重合開始剤を加え、通常0〜80℃程
度で数時間重合することにより行うことができ
る。乳化重合の場合は、たとえば特開昭50−
102388号公報に記載の方法により行うことができ
る。
The polymerization can be carried out using known methods such as aqueous solution polymerization,
It can be carried out by methods such as emulsion polymerization, suspension polymerization, and precipitation polymerization. In the case of aqueous solution polymerization, for example, monomers are added to an aqueous solution (monomer concentration is, for example, 10 to 90
After replacing the system with an inert gas, a radical polymerization initiator is added, and polymerization is carried out usually at about 0 to 80° C. for several hours. In the case of emulsion polymerization, for example,
This can be carried out by the method described in Japanese Patent No. 102388.

本発明により一般式(1)で示されるモノマーの四
級化に際する加水分解、重合等の不都合な副反応
が効果的に抑止でき、不飽和酸、重合物等の不純
物含有量の極めて低い高品質の第四級アンモニウ
ム塩モノマーの工業的製造が可能となつた。これ
は水を反応と並行して添加しながら四級化を行う
ことにより初めて達成できたものであり従来より
公知の方法では為し得なかつたものである。
According to the present invention, disadvantageous side reactions such as hydrolysis and polymerization during quaternization of the monomer represented by general formula (1) can be effectively suppressed, and the content of impurities such as unsaturated acids and polymers is extremely low. Industrial production of high quality quaternary ammonium salt monomers has become possible. This was achieved for the first time by performing quaternization while adding water in parallel with the reaction, and could not be achieved by conventionally known methods.

本発明によつて得られた第四級アンモニウム塩
モノマーは繊維処理剤、高分子疑豊剤、製紙用薬
剤、接着剤等に用いられる機能性ポリマーの原料
モノマーとして極めて有用性が高い。
The quaternary ammonium salt monomer obtained by the present invention is extremely useful as a raw material monomer for functional polymers used in fiber treatment agents, polymer enrichment agents, paper-making agents, adhesives, and the like.

以下実施例を以て本発明をさらに説明するが、
本発明はこれに限定されるものではない。
The present invention will be further explained below with reference to Examples.
The present invention is not limited to this.

実施例 1 撹拌機、温度計、滴下ロート(2個)およびサ
ンプリング管を備えた2ガラスコルベンに、ジ
メチルアミノエチルメタクリレート628g(4モ
ル)を仕込み、滴下ロートの一方に水300g、他
方にベンジルクロライド512g(4.05モル)を仕
込んだ。コルベン内の液温を25℃に調整し撹拌し
ながら水とベンジルクロライドを同時に滴下開始
し、それぞれ4時間で全量を添加した。この後更
に1時間熟成して濃度79%の第四級アンモニウム
塩水溶液1475gを得た。この間液温は外部冷却に
より25±5℃に保つた。第四級アンモニウム塩の
収率はアミン価から計算して99.8%、メタクリル
酸の副生量は使用したジメチルアミノエチルメタ
クリレートに対して0.05モル%にすぎなかつた。
また四級化反応中の重合も認めなかつた。
Example 1 628 g (4 moles) of dimethylaminoethyl methacrylate was placed in a two-glass kolben equipped with a stirrer, a thermometer, two dropping funnels, and a sampling tube, and 300 g of water was placed in one of the dropping funnels and benzyl chloride was placed in the other. 512g (4.05mol) was charged. The temperature of the liquid in the colben was adjusted to 25°C, and while stirring, water and benzyl chloride were simultaneously added dropwise, and the entire amount was added over 4 hours. Thereafter, the mixture was further aged for 1 hour to obtain 1475 g of a quaternary ammonium salt aqueous solution having a concentration of 79%. During this time, the liquid temperature was maintained at 25±5°C by external cooling. The yield of the quaternary ammonium salt was calculated from the amine value to be 99.8%, and the amount of methacrylic acid by-produced was only 0.05 mol% based on the dimethylaminoethyl methacrylate used.
Further, no polymerization was observed during the quaternization reaction.

比較例 1 実施例1で水を反応中に滴下する代りにあらか
じめ反応前に全量コルベン内に加えた点を除き他
は全く同様の条件で四級化を行つた。この場合に
はジメチルアミノエチルメタクリレートが四級化
中に加水分解し、最終的には第四級アンモニウム
塩の収率は96・0%、メタクリル酸の副生量は使
用したジメチルアミノエチルメタクリレートに対
して1.9%に達していた。また反応液はわずかに
増粘しており0.4%のポリマーを含有していた。
Comparative Example 1 Quaternization was carried out under exactly the same conditions as in Example 1, except that instead of adding water dropwise during the reaction, the entire amount was added to the kolben before the reaction. In this case, dimethylaminoethyl methacrylate is hydrolyzed during quaternization, and the final yield of quaternary ammonium salt is 96.0%, and the amount of methacrylic acid by-product is equal to the amount of dimethylaminoethyl methacrylate used. In comparison, it reached 1.9%. Additionally, the reaction solution had slightly increased viscosity and contained 0.4% polymer.

実施例2 (四級化剤と水を断続的に添加する
例) 撹拌機、温度計、滴下ロート(2個)およびサ
ンプリング管を備えた1.5リツトルのガラスオー
トクレーブにモノマーとしてジメチルアミノエチ
ルメタクリレート471g(3モル)を仕込み、滴
下ロートの一方に水156g、他方にメチルクロラ
イド153g(3.03モル)を仕込んだ。オートクレ
ーブ内の液温を20〜25℃に調整し撹拌しながらメ
チルクロライドと水を5回に分けて断続的に添加
した。この場合、添加は最初メチルクロライド30
gと水30gを30分かけて行いその後30分間熟成し
た。更に同じ方法により断続的にメチルクロライ
ドと水を添加してゆき5回目に残り全部を投入し
た後、3時間熟成して濃度80%の第四級アンモニ
ウム塩水溶液780gを得た。第四級アンモニウム
塩の収率は、アミン価から計算して99.5%、メタ
クリル酸の副生量は使用したジメチルアミノエチ
ルメタクリレートに対し0.09モル%であつた。ま
たこの場合実施例1と同じく反応中は重合は認め
られなつかた。
Example 2 (Example of intermittent addition of quaternizing agent and water) 471 g of dimethylaminoethyl methacrylate as a monomer ( One side of the dropping funnel was charged with 156 g of water, and the other was charged with 153 g (3.03 moles) of methyl chloride. The liquid temperature in the autoclave was adjusted to 20 to 25°C, and methyl chloride and water were added intermittently in five portions while stirring. In this case, the addition is initially methyl chloride 30
g and 30 g of water over 30 minutes, and then aged for 30 minutes. Further, in the same manner, methyl chloride and water were added intermittently, and after the fifth addition, the remaining mixture was added and aged for 3 hours to obtain 780 g of a quaternary ammonium salt aqueous solution with a concentration of 80%. The yield of the quaternary ammonium salt was calculated from the amine value to be 99.5%, and the amount of methacrylic acid by-produced was 0.09 mol% based on the dimethylaminoethyl methacrylate used. In this case, as in Example 1, no polymerization was observed during the reaction.

実施例3 (四級化剤と水を別添する例) 実施例2のガラスオートクレーブにモノマーと
してジメチアミノエチルアクリレート429g(3
モル)を仕込み、滴下ロートの一方に水146g、
他方にメチルクロライド153g(3.03モル)を仕
込んだ。オートクレーブ内の液温を20℃に調整し
撹拌しながらメチルクロライドを2時間で全量添
加した。この後水を連続的に2時間かけて全量滴
下した。水の添加終了後、液温を常に20±2℃に
保つて15時間熟成し、濃度80%の第四級アンモニ
ウム塩水溶液725gを得た。第四級アンモニウム
塩の収率は、アミン価から計算して99.5%、アク
リル酸の副生量は使用したジメチルアミノエチル
アクリレートに対し0.12モル%であつた。この場
合も反応中に重合は認められなつかた。
Example 3 (Example of adding quaternizing agent and water separately) 429 g of dimethyaminoethyl acrylate (3
mol), add 146g of water to one side of the dropping funnel,
On the other side, 153 g (3.03 mol) of methyl chloride was charged. The liquid temperature in the autoclave was adjusted to 20°C, and the entire amount of methyl chloride was added in 2 hours while stirring. After that, the entire amount of water was continuously added dropwise over 2 hours. After the addition of water, the solution was aged for 15 hours while keeping the temperature at 20±2° C. to obtain 725 g of a quaternary ammonium salt aqueous solution with a concentration of 80%. The yield of the quaternary ammonium salt was calculated from the amine value to be 99.5%, and the amount of acrylic acid by-produced was 0.12 mol% based on the dimethylaminoethyl acrylate used. In this case as well, no polymerization was observed during the reaction.

Claims (1)

【特許請求の範囲】 1 一般式 (式中、R1はHまたはCH3;R2,R3はそれぞ
れ独立に炭素数1〜4のアルキル基、または炭素
数2〜4のヒドロキシアルキル基;AはO(酸素
原子)またはNH、Bは炭素数1〜4のアルキレ
ン基または炭素数2〜4のヒドロキシアルキレン
基である。)で示される第三級アミノ基を有する
ビニルモノマーに四級化剤を加えて反応させて該
モノマーの第四級アンモニウム塩を製造する方法
において、反応と並行して水を断続的または連続
的に添加しながら反応を行うことを特徴とする第
四級アンモニウム塩の製造法。 2 第三級アミノ基を有するビニルモノマーに四
級化剤の添加と並行して水を断続的または連続的
に添加する特許請求の範囲第1項記載の製造法。
[Claims] 1. General formula (In the formula, R 1 is H or CH 3 ; R 2 and R 3 are each independently an alkyl group having 1 to 4 carbon atoms, or a hydroxyalkyl group having 2 to 4 carbon atoms; A is O (oxygen atom) or NH , B is an alkylene group having 1 to 4 carbon atoms or a hydroxyalkylene group having 2 to 4 carbon atoms. A method for producing a quaternary ammonium salt, characterized in that the reaction is carried out while adding water intermittently or continuously in parallel with the reaction. 2. The production method according to claim 1, wherein water is added intermittently or continuously to the vinyl monomer having a tertiary amino group in parallel with the addition of the quaternizing agent.
JP1212481A 1981-01-28 1981-01-28 Preparation of quaternary ammonium salt Granted JPS57126452A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1212481A JPS57126452A (en) 1981-01-28 1981-01-28 Preparation of quaternary ammonium salt

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1212481A JPS57126452A (en) 1981-01-28 1981-01-28 Preparation of quaternary ammonium salt

Publications (2)

Publication Number Publication Date
JPS57126452A JPS57126452A (en) 1982-08-06
JPS6318936B2 true JPS6318936B2 (en) 1988-04-20

Family

ID=11796785

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1212481A Granted JPS57126452A (en) 1981-01-28 1981-01-28 Preparation of quaternary ammonium salt

Country Status (1)

Country Link
JP (1) JPS57126452A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4745214A (en) * 1986-06-20 1988-05-17 Norsolor Process for the preparation of an aqueous solution of unsaturated quaternary ammonium salts
NL193088C (en) * 1988-02-11 1998-10-05 Norsolor Sa Process for the preparation of aqueous solutions of unsaturated quaternary ammonium salts.
US5639840A (en) * 1995-01-26 1997-06-17 Indiana University Foundation Fluoride ion releasing dental materials
KR100491098B1 (en) * 1997-10-15 2005-09-26 삼성정밀화학 주식회사 Method for preparing high purity methacrylate quaternary ammonium salt
JP4967292B2 (en) * 2005-03-07 2012-07-04 住友ベークライト株式会社 Composition, ion conductive electrolyte obtained therefrom, and secondary battery using the same

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5231017A (en) * 1975-09-03 1977-03-09 Mitsubishi Chem Ind Ltd Quaternizing process
JPS55127351A (en) * 1979-03-27 1980-10-02 Toagosei Chem Ind Co Ltd Preparation of quaternary ammonium salt monomer

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5231017A (en) * 1975-09-03 1977-03-09 Mitsubishi Chem Ind Ltd Quaternizing process
JPS55127351A (en) * 1979-03-27 1980-10-02 Toagosei Chem Ind Co Ltd Preparation of quaternary ammonium salt monomer

Also Published As

Publication number Publication date
JPS57126452A (en) 1982-08-06

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