JP2678637B2 - Polymerization method of vinyl monomer - Google Patents

Polymerization method of vinyl monomer

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Publication number
JP2678637B2
JP2678637B2 JP63268823A JP26882388A JP2678637B2 JP 2678637 B2 JP2678637 B2 JP 2678637B2 JP 63268823 A JP63268823 A JP 63268823A JP 26882388 A JP26882388 A JP 26882388A JP 2678637 B2 JP2678637 B2 JP 2678637B2
Authority
JP
Japan
Prior art keywords
polymerization
acid
acetic acid
group
aibn
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
JP63268823A
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Japanese (ja)
Other versions
JPH02115202A (en
Inventor
力 宮川
啓利 藤江
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.)
Fujifilm Wako Pure Chemical Corp
Original Assignee
Wako Pure Chemical Industries Ltd
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Priority to JP63268823A priority Critical patent/JP2678637B2/en
Publication of JPH02115202A publication Critical patent/JPH02115202A/en
Application granted granted Critical
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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/04Azo-compounds

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ビニルモノマーの効果的な重合方法に関す
る。
Description: TECHNICAL FIELD The present invention relates to a method for effectively polymerizing vinyl monomers.

〔発明の背景〕[Background of the Invention]

ビニルモノマーの重合開始剤としては、従来より過酸
化物系化合物及びアゾ系化合物が一般に良く知られてい
る。これらのうち、アゾ系重合開始剤は、総じて活性が
高いわりには比較的安定で、有機過酸化物にみられるよ
うな自己誘導分解を起さず、正確に一次反応で分解が進
行するためコントロールが容易である等の優れた特性を
有しており、種々のビニルモノマーの重合に広く用いら
れている。
Peroxide compounds and azo compounds have been generally well known as polymerization initiators for vinyl monomers. Of these, azo-based polymerization initiators are relatively stable in spite of their high activity as a whole, do not undergo the self-induced decomposition as seen in organic peroxides, and can be decomposed accurately in the primary reaction to control. It has excellent properties such as ease of use and is widely used in the polymerization of various vinyl monomers.

例えば、酢酸ビニルのメタノール溶液重合に於ける重
合開始剤としては、2,2′−アゾビスイソブチロニトリ
ル(AIBN)や2,2′−アゾビス(2−メチルプロピオン
酸メチル)等が一般に広く用いられている。しかしなが
ら、これらアゾニトリル類やアゾエステル類は重合活性
が必ずしも充分高いわけではないので、高重合率を得る
ためには長時間を要し、重合温度も比較的高い温度が要
求される。また、触媒としての添加量も必然的に多くな
るため、ポリマー中への残存触媒や分解物等の混入の問
題も生じ易い。
For example, 2,2'-azobisisobutyronitrile (AIBN), 2,2'-azobis (methyl 2-methylpropionate), etc. are generally widely used as a polymerization initiator in a methanol solution polymerization of vinyl acetate. It is used. However, since these azonitriles and azoesters do not necessarily have sufficiently high polymerization activity, it takes a long time to obtain a high polymerization rate and a relatively high polymerization temperature is required. In addition, since the amount of addition as a catalyst is inevitably large, the problem of contamination of the polymer with residual catalyst, decomposition products, and the like tends to occur.

一方、2,2′−アゾビス(2−アミジノプロパン)二
塩酸塩や、2,2′−アゾビス[2−(2−イミダゾリン
−2−イル)プロパン]二塩酸塩等のアゾアミジン塩酸
塩は上記AIBN等と比べて高重合活性を示すが、塩酸塩で
あるがために、反応設備等の腐蝕の問題があり、広く使
用されるまでには到っていない。
On the other hand, azoamidine hydrochlorides such as 2,2'-azobis (2-amidinopropane) dihydrochloride and 2,2'-azobis [2- (2-imidazolin-2-yl) propane] dihydrochloride are the above AIBN. Although it has a higher polymerization activity than that of the above, it is not yet widely used because it is a hydrochloride and therefore has a problem of corrosion of reaction equipment and the like.

また、式 で示される2,2′−アゾビス[2−(2−イミダゾリン
−2−イル)プロパン]や例えば特開昭63−115869号公
報或は特開昭63−146866号公報等に記載の各種環状アゾ
アミジン類(遊離体)は、高重合活性を有すると同時に
水及び各種有機溶媒に対する溶解性にも選れていること
から近時注目を集めているが、その効果的な使用法につ
いての検討は未だ充分なされていないと言うのが現状で
ある。
Also, the formula 2,2'-azobis [2- (2-imidazolin-2-yl) propane] represented by and various cyclic azoamidines described in, for example, JP-A-63-115869 or JP-A-63-146866. The group (free form) has been attracting attention recently because it has high polymerization activity and at the same time has been selected for its solubility in water and various organic solvents, but its effective use has not yet been examined. The current situation is that it has not been done enough.

〔発明の目的〕[Object of the invention]

本発明の目的は環状アゾアミジン化合物(遊離体)を
重合開始剤として用いたビニルモノマーのより効果的な
重合方法を提供することにある。
An object of the present invention is to provide a more effective polymerization method of a vinyl monomer using a cyclic azoamidine compound (free form) as a polymerization initiator.

〔発明の構成〕[Configuration of the invention]

本発明は、一般式[I] (式中、R1はメチル基又はエチル基を表わし、R2は水素
原子又は低級ヒドロキシアルキル基を表わし、R3は置換
基を有していてもよい低級アルキレン基を表わす。)で
示される環状アゾアミジン化合物を重合開始剤として用
い、有機酸の存在下に重合させることを特徴とするビニ
ルモノマーの重合方法である。
The present invention provides a compound represented by the general formula [I]: (In the formula, R 1 represents a methyl group or an ethyl group, R 2 represents a hydrogen atom or a lower hydroxyalkyl group, and R 3 represents a lower alkylene group which may have a substituent.) A method for polymerizing a vinyl monomer, which comprises polymerizing in the presence of an organic acid using a cyclic azoamidine compound as a polymerization initiator.

即ち、本発明者らは、上記環状アゾアミジン化合物を
重合開始剤として用いるビニルモノマーの効果的な重合
方法について鋭意研究の途上、有機酸の存在下に重合さ
せるときは、その添加につれて重合開始剤としての活性
が高くなる現象を見出し、本発明を完成させるに到っ
た。
That is, the inventors of the present invention are keenly researching an effective polymerization method of a vinyl monomer using the cyclic azoamidine compound as a polymerization initiator. The present invention has been completed by discovering a phenomenon in which the activity of is increased.

一般式[I]で示される環状アゾアミジン化合物のR1
としてはメチル基又はエチル基が挙げられ、R2としては
水素原子又は、例えばヒドロキシメチル基,ヒドロキシ
エチル基,ヒドロキシプロピル基等のヒドロシアルキル
基が挙げられ、R3としては、例えば−CH2・−CH2,−CH2
・CH2・CH2−等の如き低級アルキレン基、若しくは、こ
れら低級アルキレン基の水素原子のいくつかがメチル
基,エチル基,プロピル基,ブチル基等の低級アルキル
基又は水酸基で置き換ったものが挙げられる。
R 1 of the cyclic azoamidine compound represented by the general formula [I]
Include a methyl group or an ethyl group, R 2 includes a hydrogen atom or a hydroxyalkyl group such as a hydroxymethyl group, a hydroxyethyl group, and a hydroxypropyl group, and R 3 includes, for example, —CH 2 · -CH 2, -CH 2
.CH 2 .CH 2-, etc., or a lower alkylene group such as CH 2 --CH 2- , or some of the hydrogen atoms of these lower alkylene groups are replaced by a lower alkyl group such as a methyl group, an ethyl group, a propyl group, a butyl group or a hydroxyl group There are things.

一般式[I]で示される環状アゾアミジン化合物の代
表的な具体例を以下に構造式で示す。
Typical structural examples of the cyclic azoamidine compound represented by the general formula [I] are shown below.

これら一般式[I]で示される環状アゾアミジン化合
物は、市販品がある場合にはそれをそのまま用いればよ
いし、市販品がない場合には、例えば、特開昭56−6134
3号公報、特開昭63−115869号公報、特開昭63−146866
号公報等に記載の方法に準じて下記合成ルートによりこ
れを合成すれば良い。
As for the cyclic azoamidine compound represented by the general formula [I], when there is a commercially available product, it can be used as it is. When there is no commercially available product, for example, JP-A-56-6134 can be used.
JP-A-63-115869, JP-A-63-146866
This may be synthesized by the following synthesis route according to the method described in Japanese Patent Publication No.

(式中、R′は低級アルキル基を表わし、R1,R2及びR3
は前記と同じ。) 即ち、例えば、相当するアゾニトリルを出発物質と
し、常法に従いこれに塩化水素ガスとアルコールを反応
させてアゾイミノエーテル塩酸塩を得る。次いでこれを
適当な反応溶媒中アンモニアガスと反応させてアゾイミ
ノエーテル遊離体とした後、これに相当するジアミンを
反応させて目的の環状アゾアミジン化合物遊離体を製造
する。
(In the formula, R ′ represents a lower alkyl group, and R 1 , R 2 and R 3
Is the same as above. That is, for example, the corresponding azonitrile is used as a starting material, and hydrogen chloride gas and alcohol are reacted with this as a starting material to obtain an azoimino ether hydrochloride. Next, this is reacted with ammonia gas in an appropriate reaction solvent to obtain a free azoimino ether, and then reacted with a corresponding diamine to produce a desired free azoamidine compound.

アゾイミノエーテル遊離体とジアミン類との反応は、
通常、アゾイミノエーテル遊離体とこれに対し理論量乃
至若干過剰量のジアミンとをメタノール,エタノール等
の低級アルコール溶媒中、或はこれら低級アルコールの
存在下、他の適当な有機溶媒中、要すれば少量の酢酸を
反応促進剤として使用し室温乃至要すれば若干冷却下で
数時間乃至数日間接触させれば良く、必要に応じて撹拌
を行う等は任意である。反応後は常法に従って後処理を
行い環状アゾアミジン化合物を単離する。
The reaction between the free azoimino ether and the diamine is as follows:
Usually, the azoimino ether educt and the theoretical amount or a slight excess amount of the diamine relative to it are required in a lower alcohol solvent such as methanol or ethanol, or in the presence of these lower alcohols in another suitable organic solvent. For example, a small amount of acetic acid may be used as a reaction accelerator and contact may be carried out at room temperature or, if necessary, with slight cooling for several hours to several days, and stirring may be optionally performed. After the reaction, post-treatment is performed according to a conventional method to isolate the cyclic azoamidine compound.

本発明の方法を実施するには、上記環状アゾアミジン
化合物を重合開始剤として用い、有機酸の存在下に重合
性ビニルモノマーを重合或いは共重合させればよいわけ
であるが、ここで用いられる有機酸としては、例えばギ
酸、酢酸、プロピオン酸、マロン酸、コハク酸、乳酸、
グルタル酸、アジピン酸、粘液酸、メタンスルホン酸、
p−トルエンスルホン酸、安息香酸、アクリル酸、メタ
クリル酸等が代表的なものとして挙げられる。
In order to carry out the method of the present invention, the cyclic azoamidine compound may be used as a polymerization initiator and a polymerizable vinyl monomer may be polymerized or copolymerized in the presence of an organic acid. Examples of the acid include formic acid, acetic acid, propionic acid, malonic acid, succinic acid, lactic acid,
Glutaric acid, adipic acid, mucus acid, methanesulfonic acid,
Typical examples include p-toluenesulfonic acid, benzoic acid, acrylic acid, methacrylic acid and the like.

酸の使用量は、酸の種類や用いるモノマーの種類或は
重合方法によっても異なるが、通常用いた重合開始剤の
0.1乃至20倍モル程度(場合によってはそれ以上のこと
もある。)好ましくは0.4〜10倍モル程度を用いればよ
く、少なすぎると重合活性の向上は然程望めず、多すぎ
ると効率や経済性等の点で問題となる。
The amount of the acid used varies depending on the type of the acid, the type of the monomer used or the polymerization method.
About 0.1 to 20 times mol (may be more than that in some cases) It is preferable to use about 0.4 to 10 times mol. If it is too small, improvement of polymerization activity cannot be expected so much, and if it is too large, efficiency and economy are increased. There is a problem in terms of sex.

本発明の方法が適応可能な重合性ビニルモノマーとし
ては、例えば、各種オレフィン類、スチレン、アクリル
酸メチル、メタアクリル酸メチル、アクリロニトリル、
アクリルアミド、酢酸ビニル、塩化ビニル、ビニルピロ
リドン、ビニルピリジン、アクリル酸、メタクリル酸、
メタクリルアミド等が挙げられ、また、これらと共重合
し得るモノマーとしては、上記のビニルモノマーのほ
か、無水マレイン酸やマレイン酸、フマル酸等が挙げら
れる。
As the polymerizable vinyl monomer to which the method of the present invention is applicable, for example, various olefins, styrene, methyl acrylate, methyl methacrylate, acrylonitrile,
Acrylamide, vinyl acetate, vinyl chloride, vinyl pyrrolidone, vinyl pyridine, acrylic acid, methacrylic acid,
Methacrylamide and the like can be mentioned, and as the monomer which can be copolymerized with them, maleic anhydride, maleic acid, fumaric acid and the like can be mentioned in addition to the above vinyl monomers.

本発明に係る重合方法自体は、自体公知の重合方法に
従ってこれを行えばよく、モノマーの性質及び生成する
ポリマーの性質、用途などに応じて、それに最も適した
方法を選択し、溶液重合、乳化重合、或いは懸濁重合さ
せればよい。
The polymerization method itself according to the present invention may be carried out according to a polymerization method known per se, depending on the properties of the monomer and the properties of the polymer to be produced, the application, etc., and select the most suitable method therefor, solution polymerization, emulsification, Polymerization or suspension polymerization may be used.

以下に実施例を挙げるが、本発明はこれら実施例によ
り何等制約を受けるものではない。
Examples are described below, but the present invention is not limited by these examples.

〔実施例〕〔Example〕

実施例1. 重合開始剤として、式 で示される2,2′−アゾビス[2−(2−イミダゾリン
−2−イル)プロパン](以下、VA−061と略記す
る。)を0.187g、有機酸として酢酸を0.09g用い、これ
らを酢酸ビニル200mlと共にメタノール200mlに溶解し、
N2雰囲気下重合温度50℃で重合を行った。結果を表1及
び第1図に示す。また、比較のため、酢酸無添加の場合
及びAIBNを開始剤とした場合の結果も表1及び第1図に
併せて示す。尚、表中の数値は重合率を示す。
Example 1. As the polymerization initiator, the formula 2,87 'of 2,2'-azobis [2- (2-imidazolin-2-yl) propane] (hereinafter abbreviated as VA-061) and 0.09 g of acetic acid as an organic acid were used. Dissolved in 200 ml of methanol with 200 ml of vinyl,
Polymerization was carried out in an N 2 atmosphere at a polymerization temperature of 50 ° C. The results are shown in Table 1 and FIG. In addition, for comparison, the results when acetic acid was not added and when AIBN was used as an initiator are also shown in Table 1 and FIG. The numerical values in the table indicate the polymerization rate.

表1及び第1図から明らかなように、酢酸を添加して
重合させた場合と無添加で重合させた場合とでは、明ら
かに重合活性が異なり、酢酸を添加すると重合活性が著
しく高められることが解る。またAIBNでは酢酸の添加効
果が全く無いことが解る。
As is clear from Table 1 and FIG. 1, the polymerization activity is obviously different between the case where the acetic acid is added and the case where the acetic acid is not added, and the addition of acetic acid significantly increases the polymerization activity. Understand. Also, it can be seen that AIBN has no effect of adding acetic acid.

実施例2. VA−061を0.187g,酢酸を表2に記載の各添加量用い、
これらを酢酸ビニル200mlと共にメタノール200mlに溶解
してN2雰囲気下重合温度50℃で重合を行った。結果を表
2及び第2図に示す。尚、表中の数値は重合率を示す。
Example 2. 0.187 g of VA-061 and acetic acid were used in the respective addition amounts shown in Table 2,
These were dissolved in 200 ml of methanol together with 200 ml of vinyl acetate and polymerized at a polymerization temperature of 50 ° C. under N 2 atmosphere. The results are shown in Table 2 and FIG. The numerical values in the table indicate the polymerization rate.

表2及び第2図から明らかなように、酢酸の添加量を
増加させるにつれて重合活性が高められることが解る。
As is clear from Table 2 and FIG. 2, it is understood that the polymerization activity is increased as the addition amount of acetic acid is increased.

実施例3. VA−061及び酢酸を表3に記載の各添加量用い、これ
らを酢酸ビニル200mlと共にメタノール200mlに溶解して
N2雰囲気下重合温度50℃で重合を行った。結果を表3及
び第3図に示す。また比較のため、AIBNを用いた場合の
結果も表3及び第3図に併せて示す。尚、表中の数値は
重合率を示す。
Example 3. VA-061 and acetic acid were added in the amounts shown in Table 3 and dissolved in 200 ml of methanol together with 200 ml of vinyl acetate.
Polymerization was carried out in an N 2 atmosphere at a polymerization temperature of 50 ° C. The results are shown in Table 3 and FIG. For comparison, the results when AIBN is used are also shown in Table 3 and FIG. The numerical values in the table indicate the polymerization rate.

表3及び第3図から明らかなように酢酸を添加したVA
−061の重合活性は従来のAIBNと比べて高くAIBNを用い
た場合よりも開始剤の添加量を少なくすることができる
ことが解る。
As is clear from Table 3 and FIG. 3, VA added with acetic acid
It can be seen that the polymerization activity of −061 is higher than that of conventional AIBN and the amount of the initiator added can be reduced as compared with the case of using AIBN.

実施例4. VA−061を0.187g、酢酸を0.09g用い、これらを酢酸ビ
ニル200mlと共にメタノール200mlに溶解してN2雰囲気下
表4に記載の重合温度で重合を行った。結果を表4及び
第4図に示す。また比較のため、AIBNを用いた場合の結
果も表4及び第4図に併せて示す。尚、表中の数値は重
合率を示す。
Example 4. Using 0.187 g of VA-061 and 0.09 g of acetic acid, these were dissolved in 200 ml of methanol together with 200 ml of vinyl acetate and polymerized at a polymerization temperature shown in Table 4 under N 2 atmosphere. The results are shown in Table 4 and FIG. For comparison, the results when AIBN is used are also shown in Table 4 and FIG. The numerical values in the table indicate the polymerization rate.

表4及び第4図から明らかなように、酢酸を添加した
VA−061の重合活性は従来のAIBNと比べて高く、AIBNを
用いた場合よりも重合温度を低くすることができること
が解る。
As apparent from Table 4 and FIG. 4, acetic acid was added.
It can be seen that the polymerization activity of VA-061 is higher than that of conventional AIBN, and the polymerization temperature can be lowered as compared with the case of using AIBN.

実施例5. 重合開始剤としてVA−061を0.187g用い、有機酸とし
て表5に記載の有機酸を夫々VA−061に対して2倍モル
用いて、酢酸ビニル200mlと共にメタノール200mlに溶解
し、N2雰囲気下、重合温度50℃で重合を行った。結果を
表5及び第5図に示す。尚、表中の数値は重合率を示
す。
Example 5. 0.187 g of VA-061 was used as a polymerization initiator, and the organic acid shown in Table 5 was used as an organic acid in an amount of 2 times the moles of VA-061, respectively, and dissolved in 200 ml of methanol together with 200 ml of vinyl acetate. Polymerization was performed at a polymerization temperature of 50 ° C. in an N 2 atmosphere. The results are shown in Table 5 and FIG. The numerical values in the table indicate the polymerization rate.

表5及び第5図から明らかなように、酢酸以外の有機
酸を用いた場合も酢酸を用いた場合と同様の効果、即ち
重合活性が増大する効果が得られ、解離定数が大きな酸
ほどその効果は大きい。
As is clear from Table 5 and FIG. 5, the same effect as in the case of using acetic acid, that is, the effect of increasing the polymerization activity was obtained when an organic acid other than acetic acid was used. The effect is great.

実施例6. 重合開始剤として、式 で示される2,2′−アゾビス[2−(2−イミダゾリン
−2−イル)ブタン]を0.187g用い、有機酸としてメタ
ンスルホン酸又はp−トルエンスルホン酸を重合開始剤
に対して2倍モル用いて、酢酸ビニル200mlと共にメタ
ノール200mlに溶解し、N2雰囲気下、重合温度50℃で重
合を行った。結果を表6及び第6図に示す。尚、表中の
数値は重合率を示す。
Example 6. As a polymerization initiator, a formula 0.12 g of 2,2'-azobis [2- (2-imidazolin-2-yl) butane] represented by is used, and methanesulfonic acid or p-toluenesulfonic acid is used as an organic acid in a 2-fold molar amount with respect to the polymerization initiator. It was dissolved in 200 ml of methanol together with 200 ml of vinyl acetate and polymerized at a polymerization temperature of 50 ° C. under N 2 atmosphere. The results are shown in Table 6 and FIG. The numerical values in the table indicate the polymerization rate.

表6及び第6図から明らかな如く、VA−061以外の環
状アゾアミジン化合物を重合開始剤として用いた場合で
も有機酸の添加により重合活性の増大効果が顕著に認め
られる。
As is clear from Table 6 and FIG. 6, even when a cyclic azoamidine compound other than VA-061 is used as a polymerization initiator, the effect of increasing the polymerization activity is remarkably recognized by the addition of the organic acid.

〔発明の効果〕〔The invention's effect〕

本発明は、環状アゾアミジン化合物を重合開始剤とし
たビニルモノマーの効果的な重合方法を提供するもので
あり、本発明の方法により有機酸の存在下に重合を行っ
た場合には、AIBN等を用いる従来の方法に比べて重合活
性が著しく高められ、従来よりも少ない開始剤の量で、
従来よりも低い温度で且つ従来よりも短い重合時間で、
目的とする重合物が得られる点に顕著な効果を奏するも
のである。
The present invention provides an effective polymerization method of a vinyl monomer using a cyclic azoamidine compound as a polymerization initiator, and when the polymerization is carried out in the presence of an organic acid by the method of the present invention, AIBN or the like is added. Polymerization activity is significantly increased compared to the conventional method used, and with a smaller amount of initiator than the conventional method,
At a lower temperature and a shorter polymerization time than before,
A remarkable effect is obtained in that a desired polymer is obtained.

【図面の簡単な説明】[Brief description of the drawings]

第1図は、実施例1で得られた重合率曲線を示し、横軸
の各重合時間(hr.)に於ける重合率(%)を縦軸に沿
ってプロットした点を結んだものである。但し、−●−
は重合開始剤として2,2′−アゾビス[2−(2−イミ
ダゾリン−2−イル)プロパン](以下、VA−061と略
記する。)を用い、酢酸を添加した場合、−○−は同無
添加の場合、−■−は重合開始剤としてアゾビスイソブ
チロニトリル(AIBN)を用い酢酸を添加した場合、−□
−は同無添加の場合の結果を夫々示す。 第2図は、実施例2で得られた重合率曲線を示し、−▽
−は酢酸を20倍モル使用した場合、−□−は同10倍モル
の場合、−○−は同2倍モルの場合、−△−は同0.4倍
モルの場合、 は酢酸無添加の場合の結果を夫々示す。また、−−−−
はAIBNを重合開始剤として用いた場合(酢酸無添加)の
結果を示す。 第3図は、実施例3で得られた重合率曲線を示し、−○
−はVA−061,0.5wt%添加の場合、−□−は同0.1wt%の
場合、−4△−は同0.05wt%の場合、 は同0.02wt%の場合、−▽−は同0.01wt%の場合、−●
−はAIBN,0.5wt%添加の場合、−■−は同0.1wt%の場
合の結果を夫々示す。 第4図は、実施例4で得られた重合率曲線を示し、−○
−は重合温度50℃の場合、−□−は同45℃の場合、−△
−は同40℃の場合の結果を夫々示し、−●−は重合開始
剤としてAIBNを用い50℃で重合した場合の結果を示す。 第5図は、実施例5で得られた重合率曲線を示し、−□
−は有機酸としてp−トルエンスルホン酸を用いた場
合、 はメタンスルホン酸を用いた場合、−○−は酢酸を用い
た場合、−△−は安息香酸を用いた場合、−●−は有機
酸無添加の場合の結果を夫々示す。 第6図は、実施例6で得られた重合率曲線を示し、−○
−は有機酸としてメタンスルホン酸を用いた場合、−□
−はp−トルエンスルホン酸を用いた場合の結果を夫々
示す。
FIG. 1 shows the polymerization rate curve obtained in Example 1, which is obtained by connecting the points plotted along the vertical axis with the polymerization rate (%) at each polymerization time (hr.) On the horizontal axis. is there. However, − ● −
Is 2,2'-azobis [2- (2-imidazolin-2-yl) propane] (hereinafter abbreviated as VA-061) as a polymerization initiator, and when acetic acid is added,-○-is the same. In the case of no addition,-■-is in the case of adding acetic acid using azobisisobutyronitrile (AIBN) as a polymerization initiator.
-Indicates the results in the case of no addition. FIG. 2 shows the polymerization rate curve obtained in Example 2, where − ▽
-When acetic acid is used at 20 times mol,-□-is at 10 times mol,-○-is at 2 times mol,-△-is at 0.4 mol times, Shows the results when acetic acid was not added. Also, ---
Shows the results when AIBN was used as a polymerization initiator (without addition of acetic acid). FIG. 3 shows the polymerization rate curve obtained in Example 3, and
-In the case of adding VA-061, 0.5 wt%,-□-in the case of 0.1 wt%, -4 △-in the case of 0.05 wt%, Is the same as 0.02 wt%, − ▽ − is the same as 0.01 wt%, − ●
− Indicates the result when AIBN and 0.5 wt% were added, and − ■ − indicates the result when 0.1 wt% was added. FIG. 4 shows the polymerization rate curve obtained in Example 4, and
− Is for polymerization temperature of 50 ° C, − □ is for same temperature of 45 ° C, − △
-Indicates the results at the same temperature of 40 ° C, and- ● -indicates the results when polymerized at 50 ° C using AIBN as the polymerization initiator. FIG. 5 shows the polymerization rate curve obtained in Example 5, where − □
-In the case of using p-toluenesulfonic acid as the organic acid, Indicates the results when methanesulfonic acid was used,-○-when acetic acid was used, -Δ- when benzoic acid was used, and-●-when organic acid was not added. FIG. 6 shows the polymerization rate curve obtained in Example 6, and
-Is the case where methanesulfonic acid is used as the organic acid,-□
-Indicates the results when p-toluenesulfonic acid was used.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】一般式[I] (式中、R1はメチル基又はエチル基を表わし、R2は水素
原子又は低級ヒドロキシアルキル基を表わし、R3は置換
基を有していてもよい低級アルキレン基を表わす。)で
示される環状アゾアミジン化合物を重合開始剤として用
い、有機酸の存在下に重合させることを特徴とするビニ
ルモノマーの重合方法。
1. A compound of the general formula [I] (In the formula, R 1 represents a methyl group or an ethyl group, R 2 represents a hydrogen atom or a lower hydroxyalkyl group, and R 3 represents a lower alkylene group which may have a substituent.) A method for polymerizing vinyl monomers, which comprises polymerizing in the presence of an organic acid using a cyclic azoamidine compound as a polymerization initiator.
JP63268823A 1988-10-25 1988-10-25 Polymerization method of vinyl monomer Expired - Fee Related JP2678637B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63268823A JP2678637B2 (en) 1988-10-25 1988-10-25 Polymerization method of vinyl monomer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63268823A JP2678637B2 (en) 1988-10-25 1988-10-25 Polymerization method of vinyl monomer

Publications (2)

Publication Number Publication Date
JPH02115202A JPH02115202A (en) 1990-04-27
JP2678637B2 true JP2678637B2 (en) 1997-11-17

Family

ID=17463749

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63268823A Expired - Fee Related JP2678637B2 (en) 1988-10-25 1988-10-25 Polymerization method of vinyl monomer

Country Status (1)

Country Link
JP (1) JP2678637B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6403774B1 (en) * 2000-10-04 2002-06-11 Wako Pure Chemical Industries, Ltd. Azoamidine compound

Also Published As

Publication number Publication date
JPH02115202A (en) 1990-04-27

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