JPS5828866B2 - Stabilization method for cationic vinyl monomers - Google Patents
Stabilization method for cationic vinyl monomersInfo
- Publication number
- JPS5828866B2 JPS5828866B2 JP52112597A JP11259777A JPS5828866B2 JP S5828866 B2 JPS5828866 B2 JP S5828866B2 JP 52112597 A JP52112597 A JP 52112597A JP 11259777 A JP11259777 A JP 11259777A JP S5828866 B2 JPS5828866 B2 JP S5828866B2
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- Prior art keywords
- cationic vinyl
- vinyl monomer
- acid
- reaction
- monomer
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Description
【発明の詳細な説明】
この発明は一般式
(式中、R1は−Hまたは−CH3、R2は−Hまたは
−CH3を表わし、X○はC1−1BrCH3SO4−
または1/2S04−一を表わす。Detailed Description of the Invention This invention is based on the general formula (wherein R1 represents -H or -CH3, R2 represents -H or -CH3, and X○ represents C1-1BrCH3SO4-
Or represents 1/2S04-1.
)で示されるカチオン性ビニルモノマー(I)の安定化
法に関するものである。) This relates to a method for stabilizing the cationic vinyl monomer (I) shown in (I).
カチオン性ビニルモノマー(I)の単独重合体および該
モノマーとアクリルアマイド、ビニルピリジン塩、メチ
ルアクリレート等との共重合体は工場廃水、都市下水、
蓄産廃水等の清澄化剤、各種スラッジの脱水剤として、
あるいは製紙工業における填料歩留向上剤、紙力増強剤
として、更にはプラスチックスの改良剤、塗装改良剤と
して利用されており、これ以外にも各種の用途が約束さ
れている。Homopolymers of the cationic vinyl monomer (I) and copolymers of this monomer with acrylamide, vinylpyridine salts, methyl acrylate, etc. are used in industrial wastewater, urban sewage,
As a clarifying agent for accumulated wastewater, etc., and as a dehydrating agent for various sludges,
It is also used as a filler retention improver and paper strength enhancer in the paper manufacturing industry, as well as as a plastics improver and coating improver, and has promise for a variety of other uses.
このためカチオン性ビニルモノマー(I)は各種カチオ
ン性ポリマーの製造原料として多量の消費が見込まれて
いる。Therefore, a large amount of cationic vinyl monomer (I) is expected to be consumed as a raw material for producing various cationic polymers.
カチオン性ビニルモノマー(■)は通常下記一般式(I
I)で示される不飽和第3級アミン(II)に塩酸、硫
酸等を加えて中和したりあるいは4級化剤を加えて4級
化反応を行なわせることによって製造される。The cationic vinyl monomer (■) usually has the following general formula (I
It is produced by adding hydrochloric acid, sulfuric acid, etc. to neutralize the unsaturated tertiary amine (II) represented by I), or by adding a quaternizing agent to cause a quaternization reaction.
(式中、R1は一部または−CH3を表わす。(In the formula, R1 represents a part or -CH3.
)カチオン性ビニルモノマー(I)を上記方法により製
造する場合、通常反応溶媒として水あるいは非水溶媒が
用いられる。) When producing the cationic vinyl monomer (I) by the above method, water or a non-aqueous solvent is usually used as the reaction solvent.
水を溶媒として用いる場合は通常、反応終了後、目的生
成物(カチオン性ビニルモノマー(I))が水に均一に
溶解しているような低濃度状態、或いは目的生成物の一
部が結晶として析出するような高濃度スラリー状態で反
応させ、一方非水溶媒中で反応を行なわせる場合は反応
終了後、反応混合物より生成結晶を分離して目的生成物
を得る方法が行なわれている。When water is used as a solvent, after the reaction is completed, the target product (cationic vinyl monomer (I)) is usually dissolved in water at a low concentration, or a part of the target product is in the form of crystals. When the reaction is carried out in a highly concentrated slurry state that causes precipitation, on the other hand, when the reaction is carried out in a non-aqueous solvent, the desired product is obtained by separating the formed crystals from the reaction mixture after the reaction is completed.
いずれの方法を採るにせよ、得られたカチオン性ビニル
モノマー(■)は原料である不飽和第3級アミン(n)
にくらべて不安定で重合し易く、特に水溶液中において
高濃度で反応させる場合は反応中あるいは貯蔵中に自然
重合を起し易い。Whichever method is used, the obtained cationic vinyl monomer (■) is the unsaturated tertiary amine (n) which is the raw material.
It is unstable and polymerizes easily compared to other materials, and spontaneous polymerization tends to occur during the reaction or storage, especially when reacting at high concentration in an aqueous solution.
非水溶媒中で反応させて得られたカチオン性ビニルモノ
マー(I)は比較的安定であるが、しかしそれでも反応
後、溶媒を回収する工程および該モノマーを乾燥する工
程で重合を起し易い。Although the cationic vinyl monomer (I) obtained by reaction in a non-aqueous solvent is relatively stable, it is still susceptible to polymerization in the step of recovering the solvent and drying the monomer after the reaction.
このようにカチオン性ビニルモノマー(I)が自然重合
を起すと、該モノマー中に不溶性ポリマーが混入したり
、該モノマーを重合させる際に適正濃度に希釈すること
や重合開始剤を混合することができなくなるため正常な
重合を行なわせることができなくなるなど商品価値は殆
んどなくなる。When the cationic vinyl monomer (I) undergoes spontaneous polymerization in this way, insoluble polymers may be mixed into the monomer, and it may be difficult to dilute the monomer to an appropriate concentration or mix a polymerization initiator when polymerizing the monomer. Since it becomes impossible to carry out normal polymerization, the commercial value is almost lost.
このような自然重合を防止するため従来ハイドロキノン
モノメチルエーテル、ハイドロキノン、フェノチアジン
、N−ニトロンフェニルヒドロキシルアミンなどが安定
剤としてカチオン性ビニルモノマー(I)に添加されて
いる。In order to prevent such spontaneous polymerization, hydroquinone monomethyl ether, hydroquinone, phenothiazine, N-nitrone phenylhydroxylamine, etc. have conventionally been added to the cationic vinyl monomer (I) as a stabilizer.
こ(7)5ち、ハイドロキノンモノメチルエーテルは最
も代表的な安定剤であるが、カチオン性ビニルモノマー
(■)に対して1000 ppm以上の量を用いてもま
だ完全に該モノマーの自然重合を防止することはできな
い。(7) 5. Hydroquinone monomethyl ether is the most typical stabilizer, but even when used in an amount of 1000 ppm or more relative to the cationic vinyl monomer (■), it still completely prevents the spontaneous polymerization of the monomer. I can't.
一方、充分な効果を得るため多量の安定剤を加えること
はカチオン性ビニルモノマー(I)の正常な重合を阻害
するので決して好ましくない上、この種の安定剤は必要
以上に多く添加してもカチオン性ビニルモノマー(I)
の安定性は必らずしも向上しないことが明らかにされて
いる。On the other hand, adding a large amount of stabilizer to obtain a sufficient effect is not at all preferable as it inhibits the normal polymerization of the cationic vinyl monomer (I), and it is also not desirable to add more stabilizers than necessary. Cationic vinyl monomer (I)
It has been shown that the stability of
ハイドロキノンおよびフェノチアジンはハイドロキノン
モノメチルエーテルより安定剤としての効果は大きいが
それでもカチオン性ビニルモノマー(■)に対して数百
ppm以上添加しないと充分な効果が得られないばかり
かこのように多量用いるとカチオン性ビニルモノマー(
I)の着色が著しく、かつこれを重合させた場合にポリ
マーは褐色ないしは黒褐色に着色して商品価値を著しく
傷つげてしまう。Hydroquinone and phenothiazine are more effective as stabilizers than hydroquinone monomethyl ether, but even so, sufficient effects cannot be obtained unless they are added in amounts of several hundred ppm or more to the cationic vinyl monomer (■). vinyl monomer (
The coloration of I) is significant, and when it is polymerized, the polymer is colored brown or blackish brown, significantly damaging its commercial value.
N−40ソフエニルヒドロキシルアミンはハイドロキノ
ン等にくらべて安定剤としての効果は格段に大きく、通
常カチオン性ビニルモノマー(I)に対して数ppm〜
数十ppmの添加で充分である。N-40 sophenylhydroxylamine is much more effective as a stabilizer than hydroquinone, etc., and is usually used in amounts of several ppm to cationic vinyl monomer (I).
Addition of several tens of ppm is sufficient.
しかし、このものもごく少量添加しただけでカチオン性
ビニルモノマー(■)を着色させる傾向があり、更にこ
れを不飽和第3級アミン(II)を硫酸で中和して得ら
れるモノマーのように特に自然重合し易いものの製造、
貯蔵時に用いた場合は前記添加量では不充分であってよ
り多量の添加を必要とする。However, this substance also has a tendency to color the cationic vinyl monomer (■) even when added in a very small amount, and furthermore, it can be used as a monomer obtained by neutralizing unsaturated tertiary amine (II) with sulfuric acid. Production of materials that are particularly prone to spontaneous polymerization,
When used during storage, the amount added is insufficient and a larger amount is required.
この結果、カチオン性ビニルモノマ−(I)の重合が著
しく阻害さ、れ、たとえばこれを重合させる場合に重合
が途中で停止して残存モノマーの多いポリマーが生威し
易くなったり、重合の際非常に長い誘導期と長い重合時
間を必要とするようになったりすることが起る。As a result, the polymerization of the cationic vinyl monomer (I) is significantly inhibited, and for example, when polymerizing it, the polymerization may stop midway and a polymer with a large amount of residual monomers may easily grow, or there may be problems during polymerization. This may require a long induction period and a long polymerization time.
コノようなことから、カチオン性ビニルモノマー(I)
の自然重合を防止する効果が優れているだけではなく、
該モノマーを重合させた場合にそのコントロールが容易
でしかも重合物を着色させないような安定剤が従来より
要望されている。From this fact, the cationic vinyl monomer (I)
Not only is it highly effective in preventing the spontaneous polymerization of
There has been a demand for a stabilizer which can be easily controlled when the monomer is polymerized and which does not cause coloring of the polymerized product.
本発明者らはかかる要望に応えたカチオン性ビニルモノ
マー(I)の安定剤を見出すべく鋭意研究した結果、シ
ュウ酸、クエン酸、リンゴ酸、縮合リン酸およびこれら
の塩類がその目的に適った優れた安定剤であることを見
出し本発明に到達した。The present inventors conducted intensive research to find a stabilizer for the cationic vinyl monomer (I) that met these demands, and found that oxalic acid, citric acid, malic acid, condensed phosphoric acid, and salts thereof were suitable for the purpose. We have discovered that it is an excellent stabilizer and have arrived at the present invention.
すなわち本発明は一般式
(式中、R1は−Hまたは−CH3、R2は−Hまたは
−CH3を表わし、xeはCl−1BrCH3SO,:
または1/2S04−一を表わす。That is, the present invention is based on the general formula (wherein R1 represents -H or -CH3, R2 represents -H or -CH3, and xe represents Cl-1BrCH3SO,
Or represents 1/2S04-1.
)で示されるカチオン性ビニルモノマー(■)に、安定
剤としてシュウ酸、クエン酸、リンゴ酸、縮合リン酸お
よびこれらの塩類からなる群から選ばれた少なくとも1
種を用いることを特徴とするカチオン性ビニルモノマー
の安定化法に係るものである。), at least one stabilizer selected from the group consisting of oxalic acid, citric acid, malic acid, condensed phosphoric acid, and salts thereof.
The present invention relates to a method for stabilizing cationic vinyl monomers characterized by using seeds.
本発明に用いる縮合リン酸とは一般式、
Hn+2PnO3n+1および(I−IPO3)n(但
し、nは2以上の整数)で表わされる化合物であって、
その好適なものとしてl・リリン酸、ピロリン酸、トリ
メタリン酸、テトラメタリン酸、トリポリリン酸、ヘキ
サメタリン酸などが挙げられる。The condensed phosphoric acid used in the present invention is a compound represented by the general formula: Hn+2PnO3n+1 and (I-IPO3)n (where n is an integer of 2 or more),
Suitable examples thereof include l-lyphosphoric acid, pyrophosphoric acid, trimetaphosphoric acid, tetrametaphosphoric acid, tripolyphosphoric acid, and hexametaphosphoric acid.
また本発明に用いるシュウ酸、クエン酸、リンゴ酸およ
び縮合リン酸の塩とはそれぞれの酸のアルカリ金属塩、
アンモニウム塩および水溶性のアミン塩であって、好適
なものとして、シュウ酸、クエン酸およびリンゴ酸のそ
れぞれのナトリウム塩、カリウム塩およびアンモニウム
塩、ジメチルアミノエタノールシュウ酸塩、トリポリリ
ン酸ソーダおよびヘキサメタリン酸ソーダなどが挙げら
れる。In addition, the salts of oxalic acid, citric acid, malic acid and condensed phosphoric acid used in the present invention are the alkali metal salts of the respective acids,
Ammonium salts and water-soluble amine salts, such as the respective sodium, potassium and ammonium salts of oxalic, citric and malic acids, dimethylaminoethanol oxalate, sodium tripolyphosphate and hexametaphosphate. Examples include soda.
これら安定剤のカチオン性ビニルモノマー(I)に対す
る添加量は安定剤の種類によって異なるが、通常、モノ
マーに対して0.1〜5000 ppm、好ましくは0
.5〜2000 ppm添加する。The amount of these stabilizers added to the cationic vinyl monomer (I) varies depending on the type of stabilizer, but is usually 0.1 to 5000 ppm, preferably 0.
.. Add 5-2000 ppm.
本発明に用いる安定剤はカチオン性ビニルモノマー(I
)に通常少量添加するだけで有効なので該モノマーを重
合させる場合にその重合挙動を阻害することが少なく、
さらに本発明に用いる安定剤は一般に多量生産されてい
て安価に入手し得るのでカチオン性ビニルモノマー(I
)の製造コストを低減することができる上、該モノマー
およびその重合物の外観・色調を損うことがない。The stabilizer used in the present invention is a cationic vinyl monomer (I
), it is effective just by adding a small amount to the monomer, so it hardly inhibits the polymerization behavior when polymerizing the monomer.
Furthermore, the stabilizer used in the present invention is generally produced in large quantities and can be obtained at low cost, so the cationic vinyl monomer (I
) can reduce the manufacturing cost, and the appearance and color tone of the monomer and its polymer are not impaired.
なお、これらの安定剤をカチオン性ビニルモノマー(I
)に添加するに当り、従来公知の安定剤を併用しても差
支えなく、併用により相剰効来が認められる場合が多い
。In addition, these stabilizers are combined with cationic vinyl monomer (I
), conventionally known stabilizers may be used in combination, and mutual effects are often observed when used in combination.
たとえばハイドロキノンモノメチルエーテルが既に添加
されているカチオン性ビニルモノマー(I)に少量のシ
ュウ酸を加えることにより各単独添加の場合にくらべて
該モノマーの貯蔵安定性を高めることができる。For example, by adding a small amount of oxalic acid to the cationic vinyl monomer (I) to which hydroquinone monomethyl ether has already been added, the storage stability of the monomer can be increased compared to the case where each monomer is added alone.
本発明に用いるカチオン性ビニルモノマー(I)は既述
の一般式(TI)で示されるジメチルアミノエチル(メ
タ)アクリレート類の塩および4級アミン塩であって、
より具体的に示せばジメチルアミノエチル(メタ)アク
リレートの硫酸塩、塩酸塩、ジメチル硫酸4級塩、メチ
ルクロライド4級塩、メチルブロマイド4級塩などが挙
げられる。The cationic vinyl monomer (I) used in the present invention is a salt of dimethylaminoethyl (meth)acrylate and a quaternary amine salt represented by the general formula (TI) described above,
More specifically, examples include dimethylaminoethyl (meth)acrylate sulfate, hydrochloride, dimethyl sulfate quaternary salt, methyl chloride quaternary salt, methyl bromide quaternary salt, and the like.
これらのカチオン性ビニルモノマー(I)の殆んどのも
のはそれ自体結晶形であるが、水には非常によく溶解し
、一般に室温で401’/lo。Although most of these cationic vinyl monomers (I) are themselves in crystalline form, they are very soluble in water, generally 401'/lo at room temperature.
r水以上の溶解度を示す。r Shows solubility higher than water.
このためこれらモノマーは非常に高濃度の水溶液状態で
製造することが可能である。Therefore, these monomers can be produced in the form of very highly concentrated aqueous solutions.
これらモノマーを水溶液中で製造する場合、モノマー濃
度が低い場合にはモノマーは比較的安定であるが、濃度
が高くたとえば50重量%以上の高濃度になると安定性
が失なわれて自然重合を起し易くなる。When these monomers are produced in an aqueous solution, they are relatively stable when the monomer concentration is low, but when the concentration is high, for example 50% by weight or more, stability is lost and spontaneous polymerization occurs. It becomes easier to do.
したがって本発明に用いる安定剤はカチオン性ビニルモ
ノマー(■)を水溶液中において50重量%以上の濃度
で製造するような場合に特に適切な安定剤であり、優れ
た効果が得られる。Therefore, the stabilizer used in the present invention is particularly suitable when the cationic vinyl monomer (■) is produced in an aqueous solution at a concentration of 50% by weight or more, and excellent effects can be obtained.
カチオン性ビニルモノマー(I)は低級アルコールを除
き殆んどの有機溶媒にはあまり溶解しない。The cationic vinyl monomer (I) is poorly soluble in most organic solvents except lower alcohols.
したがって該モノマーを結晶状で得る場合は、たとえば
アセトニトリルのような有機溶媒中で不飽和第3級アミ
ンと4級化剤等を反応させ、生成結晶をp過分離する方
法が通常行なわれているが、この場合、反応中だけでは
なく、反応混合物より汗別した結晶を乾燥する工程ある
いは涙液より有機溶媒を回収する工程でカチオン性ビニ
ルモノマー(■)が重合を起し易い。Therefore, in order to obtain the monomer in crystal form, the usual method is to react an unsaturated tertiary amine with a quaternizing agent or the like in an organic solvent such as acetonitrile, and then perform p-perisolation of the resulting crystals. However, in this case, the cationic vinyl monomer (■) tends to polymerize not only during the reaction but also during the step of drying the crystals separated from the reaction mixture or the step of recovering the organic solvent from the tear fluid.
本発明における安定剤はこのような場合の各工程に適用
することによっても優れた効果を発揮する。The stabilizer in the present invention exhibits excellent effects when applied to each step in such cases.
なお、叙上のカチオン性ビニルモノマー(I)の水溶液
中での製造反応および非水溶媒中での製造反応は通常室
温から150℃の範囲で行なわれるが、あまり高い温度
で行なうと、原料不飽和第3級アミンの重合を併発する
恐れがあるのでこれを極力防止するため一般に約80℃
以上で反応させることが好ましい。Note that the production reaction of the cationic vinyl monomer (I) in an aqueous solution and in a non-aqueous solvent is usually carried out at a temperature ranging from room temperature to 150°C, but if carried out at too high a temperature, raw materials may be lost. Generally, the temperature is about 80°C to prevent polymerization of saturated tertiary amine as much as possible.
It is preferable to carry out the reaction in the above manner.
叙上の説明から明らかなように本発明方法は単にカチオ
ン性ビニルモノマー(I)を貯蔵する場合だけに適用さ
れるのではなく、該モノマーを製造する際に用いること
により従来よりも有利に該モノマーを製造することがで
きる。As is clear from the above description, the method of the present invention is not only applicable to the storage of cationic vinyl monomer (I), but also can be used to produce the monomer more advantageously than before. Monomers can be produced.
次に実施例および比較例を用いて本発明を説明☆☆する
。Next, the present invention will be explained using Examples and Comparative Examples.
実施例1〜5
ジメチルアミノエチルメタクリレート6331を内容1
tのビーカーに入れ、次いで第1表に記載の安定剤を加
え、攪拌しながら濃度53.7重量%の硫酸水溶液36
7Zを10分間で滴下した。Examples 1-5 Dimethylaminoethyl methacrylate 6331 content 1
Then, add the stabilizer listed in Table 1, and add the sulfuric acid aqueous solution 36 with a concentration of 53.7% by weight while stirring.
7Z was added dropwise over 10 minutes.
硫酸水溶液の滴下中は中和熱を除去するためビーカーを
外側から冷却した。During the dropping of the sulfuric acid aqueous solution, the beaker was cooled from the outside to remove the heat of neutralization.
滴下中、反応温度が60℃を越えることはなかった。During the dropwise addition, the reaction temperature never exceeded 60°C.
反応終了後、反応混合物を室温に冷却し、硫酸水溶液滴
下終了時を起点にして反応生成物(ジメチルアミノエチ
ルメタクリレート硫酸塩)の重合が起り始まるまでの時
間と反応生成物の着色の有無を測定した。After the reaction is completed, the reaction mixture is cooled to room temperature, and the time until the reaction product (dimethylaminoethyl methacrylate sulfate) begins to polymerize starting from the end of dropping the sulfuric acid aqueous solution and the presence or absence of coloration of the reaction product are measured. did.
反応生成物の重合開始点は反応混合物にガラス棒を浸漬
して引き上げたときに糸引き現象を示す点とした。The polymerization initiation point of the reaction product was determined as the point at which a glass rod was immersed in the reaction mixture and exhibited a stringy phenomenon when pulled up.
得られた結果を第1表に示す。The results obtained are shown in Table 1.
比較例1〜9
実施例1〜3で用いたのと同じ装置を用い、同じ方法で
ジメチルアミノエチルメタクリレートの硫酸中和を行な
った。Comparative Examples 1 to 9 Dimethylaminoethyl methacrylate was neutralized with sulfuric acid using the same apparatus and method as used in Examples 1 to 3.
但し、安定剤として第2表に記載のような化合物の各単
独500 ppmを用いた。However, 500 ppm of each of the compounds listed in Table 2 was used as a stabilizer.
反応後、得られた反応生成物について実施例1〜3の場
合と同じ試験をした。After the reaction, the obtained reaction products were subjected to the same tests as in Examples 1-3.
得られた結果を第2表に示す。The results obtained are shown in Table 2.
第2表から明らかなように、従来公知の化合物(比較例
1〜4)および本発明に用いる有機酸と類似の有機酸(
比較例5〜9)を安定剤としてジメチルアミノエチルメ
タクリレートの硫酸中和を行なった場合には、反応生成
物は比較的短期間のうちに重合を起す。As is clear from Table 2, conventionally known compounds (Comparative Examples 1 to 4) and organic acids similar to the organic acids used in the present invention (
When dimethylaminoethyl methacrylate was neutralized with sulfuric acid using Comparative Examples 5 to 9) as a stabilizer, the reaction product polymerized within a relatively short period of time.
実施例 6
還流冷却器、攪拌器、温度計、ガス導入管を付した内容
1tの反応容器に、605zのジメチルアミノエチルメ
タクリレート、201’の純水、0.05Pのシュウ酸
および1ノのハイドロキノンモノメチルエーテルを加え
、フラスコ内を55〜65℃の温度に保持しつつ攪拌下
にガス導入管より塩化メチルガスを約0.517分の流
速で導入した。Example 6 In a 1 ton reaction vessel equipped with a reflux condenser, a stirrer, a thermometer, and a gas inlet tube, 605z of dimethylaminoethyl methacrylate, 201' of pure water, 0.05P of oxalic acid, and 1 of hydroquinone were added. Monomethyl ether was added, and methyl chloride gas was introduced from the gas introduction tube at a flow rate of about 0.517 minutes while stirring while maintaining the temperature inside the flask at 55 to 65°C.
反応混合物中への塩化メチルガスの吸収を容易にするた
め反応中は反応混合物を強く攪拌する。The reaction mixture is vigorously stirred during the reaction to facilitate absorption of methyl chloride gas into the reaction mixture.
塩化メチルガスを約190S’導入した時点で反応混合
物は透明になったが更に20分間ガスの導入を続げた。The reaction mixture became transparent after about 190 S' of methyl chloride gas was introduced, but the gas was continued to be introduced for an additional 20 minutes.
この反応によりメタクリロイルオキシエチルトリメチル
アンモニウムクロライドの80%水溶液が約1ky得ら
れた。This reaction yielded about 1 ky of an 80% aqueous solution of methacryloyloxyethyltrimethylammonium chloride.
次いで該水溶液を室温で6ノ月間放置したが何等自然重
合の徴候は認められなかった。The aqueous solution was then allowed to stand at room temperature for 6 months, but no signs of spontaneous polymerization were observed.
6ノ月間放置後、モノマー濃度を水で30%に希釈し公
知の重合開始剤を添加して水溶液重合な試みたところ放
置前と全く同じ重合挙動を示した。After standing for 6 months, the monomer concentration was diluted to 30% with water and a known polymerization initiator was added to attempt aqueous solution polymerization, which showed exactly the same polymerization behavior as before standing.
実施例 7
シュウ酸を添加しなかった以外はすべて実施例6と同じ
装置を用い、同じ方法にしたがいメタクリロイルオキシ
エチルトリメチルアンモニウムクロライドの80%水溶
液約1kgを得た。Example 7 Approximately 1 kg of an 80% aqueous solution of methacryloyloxyethyltrimethylammonium chloride was obtained using the same equipment as in Example 6 and following the same method except that oxalic acid was not added.
次いで該水溶液に安定剤としてヘキサメタリン酸ソーダ
0.02Pを添加混合したのち室温で6ノ月間放置した
が何等自然重合の徴候は認められなかった。Next, 0.02 P of sodium hexametaphosphate was added as a stabilizer to the aqueous solution, and the mixture was left to stand at room temperature for 6 months, but no signs of spontaneous polymerization were observed.
一方、ヘキサメタリン酸ソーダを添加しないで放置した
場合は1ノ月後自然重合が認められた。On the other hand, when the mixture was left without adding sodium hexametaphosphate, spontaneous polymerization was observed after one month.
実施例8〜11および比較例10−12
ジメチルアミノエチルアクリレ−)595Pを内容1t
のビーカニに入れ、次いで第3表に記載の安定剤を加え
、攪拌しながら、濃度50重量%の硫酸水溶液405?
を15分間で滴下した。Examples 8 to 11 and Comparative Example 10-12 1 t of dimethylaminoethyl acrylate) 595P
Then, add the stabilizer listed in Table 3, and while stirring, add a 50% by weight aqueous sulfuric acid solution 405?
was added dropwise over 15 minutes.
硫酸水溶液の滴下中は中和熱を除去するためビーカーを
外側から冷却した。During the dropping of the sulfuric acid aqueous solution, the beaker was cooled from the outside to remove the heat of neutralization.
滴下中、反応温度が50℃を越えることはなかった。During the dropwise addition, the reaction temperature never exceeded 50°C.
反応終了後、反応混合物を室温に冷却し、硫酸水溶液滴
下時を起点にして反応生成物(ジメチルアミノエチルア
クリレート硫酸塩)の重合が起り始めるまでの時間を測
定した。After the reaction was completed, the reaction mixture was cooled to room temperature, and the time from when the aqueous sulfuric acid solution was added dropwise until the reaction product (dimethylaminoethyl acrylate sulfate) started to polymerize was measured.
Claims (1)
マーの濃度50重量%以上の水溶液に、安定剤としてシ
ュウ酸、クエン酸、リンゴ酸、縮合リン酸およびこれら
の塩からなる群から選ばれた少なくとも1種を添加する
ことを特徴とするカチオン性ビニルモノマーの安定化法
。 (式中、R1は−Hまたは−CH3、R2は−Hまたは
−CH3を表わし、xeはCl−1BrCH3SO4−
または1/2SO4−一を表わす。 )2 シュウ酸、クエン酸、リンゴ酸、および縮合リン
酸の塩がアルカリ金属塩、アンモニウム塩および水溶性
のアミン塩である特許請求の範囲第1項記載の安定化法
。 3 カチオン性ビニルモノマーに対する安定剤の添加量
が0.1〜5000 ppmである特許請求の範囲第1
項記載の安定化法。[Claims] 1. An aqueous solution of a cationic vinyl monomer represented by the following general formula (I) with a concentration of 50% by weight or more, containing oxalic acid, citric acid, malic acid, condensed phosphoric acid, and salts thereof as stabilizers. A method for stabilizing a cationic vinyl monomer, which comprises adding at least one member selected from the group consisting of: (In the formula, R1 represents -H or -CH3, R2 represents -H or -CH3, xe represents Cl-1BrCH3SO4-
Or represents 1/2SO4-1. )2 The stabilization method according to claim 1, wherein the salts of oxalic acid, citric acid, malic acid, and condensed phosphoric acid are alkali metal salts, ammonium salts, and water-soluble amine salts. 3. Claim 1, wherein the amount of stabilizer added to the cationic vinyl monomer is 0.1 to 5000 ppm.
Stabilization method described in section.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP52112597A JPS5828866B2 (en) | 1977-09-21 | 1977-09-21 | Stabilization method for cationic vinyl monomers |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP52112597A JPS5828866B2 (en) | 1977-09-21 | 1977-09-21 | Stabilization method for cationic vinyl monomers |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5446711A JPS5446711A (en) | 1979-04-12 |
JPS5828866B2 true JPS5828866B2 (en) | 1983-06-18 |
Family
ID=14590713
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP52112597A Expired JPS5828866B2 (en) | 1977-09-21 | 1977-09-21 | Stabilization method for cationic vinyl monomers |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5828866B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6081202A (en) * | 1983-10-08 | 1985-05-09 | Nitto Chem Ind Co Ltd | Polymerization inhibitor for basic vinyl monomer |
JP2548051B2 (en) * | 1991-05-22 | 1996-10-30 | 日東化学工業株式会社 | Stabilization method of acrylamide aqueous solution |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49124017A (en) * | 1973-03-31 | 1974-11-27 |
-
1977
- 1977-09-21 JP JP52112597A patent/JPS5828866B2/en not_active Expired
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49124017A (en) * | 1973-03-31 | 1974-11-27 |
Also Published As
Publication number | Publication date |
---|---|
JPS5446711A (en) | 1979-04-12 |
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