JPS6234901A - Dispersing agent for emulsion polymerization - Google Patents

Dispersing agent for emulsion polymerization

Info

Publication number
JPS6234901A
JPS6234901A JP17407985A JP17407985A JPS6234901A JP S6234901 A JPS6234901 A JP S6234901A JP 17407985 A JP17407985 A JP 17407985A JP 17407985 A JP17407985 A JP 17407985A JP S6234901 A JPS6234901 A JP S6234901A
Authority
JP
Japan
Prior art keywords
copolymer
isobutylene
emulsion polymerization
anhydride
maleic acid
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
JP17407985A
Other languages
Japanese (ja)
Other versions
JPH0130842B2 (en
Inventor
Hidetoshi Shimada
英俊 島田
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.)
Idemitsu Petrochemical Co Ltd
Original Assignee
Idemitsu 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 Idemitsu Petrochemical Co Ltd filed Critical Idemitsu Petrochemical Co Ltd
Priority to JP17407985A priority Critical patent/JPS6234901A/en
Publication of JPS6234901A publication Critical patent/JPS6234901A/en
Publication of JPH0130842B2 publication Critical patent/JPH0130842B2/ja
Granted legal-status Critical Current

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  • Polymerisation Methods In General (AREA)

Abstract

PURPOSE:To provide the titled dispersing agent composed of a copolymer of isobutylene, maleic acid ( or its anhydride) and styrenesulfonic acid salt and capable of improving the dispersibility of monomer and giving stable emulsion when applied to the emulsion when applied to the emulsion polymerization of a vinyl monomer. CONSTITUTION:A copolymer of isobutylene, maleic acid (or its anhydride) and styrene is produced e.g. by reacting 1mol of isobutylene, 0.5-5mol of maleic acid or its anhydride and 0.01-5mol of styrene optionally in a solvent such as nitromethane in the presence of a catalyst such as benzyl peroxide, preferably at 45-150 deg.C for 1-10hr. The copolymer is sulfonated and converted to a sulfonic acid salt to obtain the objective copolymer of isobutylene, maleic acid (or its anhydride) and styrenesulfonic acid salt useful as a dispersing agent. USE:Useful in the field for producing a vinyl polymer useful as a raw material of paper and wood-processing agent, adhesive, etc.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は乳化重合用分散剤に関し、さらに詳しくは、と
くに、ビニル系モノマーの乳化重合法に使用して、千ツ
マ−の分散性を向上せしめ、かつ、安定な乳化状態の重
合乳化物を生成しうる乳化重合用分散剤に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a dispersant for emulsion polymerization, and more particularly, it is used in an emulsion polymerization method for vinyl monomers to improve the dispersibility of 1,000 yen. The present invention relates to a dispersant for emulsion polymerization that can produce a polymer emulsion in a stable and stable emulsified state.

[従来技術] 乳化重合法は、酢酸ビニル、塩化ビニルなどのビニル系
モノマーの重合法として重用されているものである。こ
の重合法は、水を媒体として反応が進められるので、上
述のビニル系モノマーのような水に不溶性のものの重合
に際しては、水中にモノマー、重合開始剤、界面活性剤
とともに乳化重合用分散剤を添加することによりモノマ
ーの分散性を向上せしめることが一般的である。
[Prior Art] The emulsion polymerization method is heavily used as a method for polymerizing vinyl monomers such as vinyl acetate and vinyl chloride. In this polymerization method, the reaction proceeds using water as a medium, so when polymerizing water-insoluble substances such as the above-mentioned vinyl monomer, a dispersant for emulsion polymerization is added together with the monomer, polymerization initiator, and surfactant in water. It is common to improve the dispersibility of monomers by adding them.

かかる乳化重合用分散剤としては、従来、無水マレイン
酸−イソブチレン共重合体のアルカリ中和物が知られて
いる。
As such a dispersant for emulsion polymerization, an alkali neutralized product of a maleic anhydride-isobutylene copolymer is conventionally known.

[発明が解決しようとする問題点] しかしながら、このものを使用して上記のビニル系モノ
マーの乳化重合を行なった場合、モノマーの水中への分
散性があまり良好でないため重合反応が円滑に進行せず
、さらには、得られた重合乳化物の安定性も低いという
問題があった。
[Problems to be Solved by the Invention] However, when this product is used to carry out the emulsion polymerization of the above-mentioned vinyl monomer, the polymerization reaction cannot proceed smoothly because the dispersibility of the monomer in water is not very good. Furthermore, there was a problem that the stability of the obtained polymer emulsion was low.

本発明は、従来のかかる問題を解消し、とくに、ビニル
系モノマーの乳化重合反応に使用して、水中でのモノマ
ーの分散性を向上せしめ、さらに、得られる重合乳化物
の安定性を高めることが可能な乳化重合用分散剤の提供
を目的とする。
The present invention solves such conventional problems, and is particularly applicable to the emulsion polymerization reaction of vinyl monomers to improve the dispersibility of the monomers in water, and furthermore to improve the stability of the resulting polymerized emulsion. The purpose of the present invention is to provide a dispersant for emulsion polymerization that is capable of

[問題点を解決するための手段] 本発明者は、上記目的を解消すべく鋭意研究を重ねた結
果、乳化重合用分散剤を構成する共重合体として、従来
の無水マレイン酸−インブチレン共重合体に、さらに第
3共重合成分としてスチレンスルホン酸塩を導入した3
元共重合体を採用することにより優れた効果が得られる
ことを確認して本発明を完成するに到った。
[Means for Solving the Problems] As a result of extensive research in order to solve the above object, the present inventor has developed a conventional maleic anhydride-imbutylene copolymer as a copolymer constituting a dispersant for emulsion polymerization. 3 in which styrene sulfonate was further introduced into the polymer as a third copolymerization component.
The present invention was completed after confirming that excellent effects can be obtained by employing the original copolymer.

すなわち、本発明の乳化重合用分散剤は、インブチレン
−マレイン酸もしくはその無水物−スチレンスルホン酸
塩からなることを特徴とする。
That is, the dispersant for emulsion polymerization of the present invention is characterized by comprising inbutylene-maleic acid or its anhydride-styrene sulfonate.

[具体的説明] 本発明の乳化重合用分散剤は、前述したように、イソブ
チレン、マレイン酸もしくはその無水物およびスチレン
スルホン酸塩を共重合成分とする3元共重合体であり、
このものは、とくに、ビニル系モノマーの乳化重合反応
に使用して有用なものである。
[Specific Description] As mentioned above, the dispersant for emulsion polymerization of the present invention is a ternary copolymer containing isobutylene, maleic acid or its anhydride, and styrene sulfonate as copolymerization components,
This product is particularly useful for emulsion polymerization reactions of vinyl monomers.

この3元共重合体の共重合成分のうちの1つはマレイン
酸もしくその無水物であるが、これに限るものではなく
、この他に、マレイン酸七ノエステル、マレイン酸ジエ
ステル、マレイン酸イミドもしくはN−置換マレイン酸
イミドなどのマレイン酸誘導体を使用することもできる
One of the copolymerization components of this ternary copolymer is maleic acid or its anhydride, but it is not limited to this.In addition, maleic acid heptanoester, maleic acid diester, maleic acid imide Alternatively, maleic acid derivatives such as N-substituted maleic acid imide can also be used.

一方、その他の共重合成分であるスチレンスルホン酸塩
としてはとくに限定されるものではないが、例えばナト
リウム塩、カリウム塩などのアルカリ金属塩は好ましい
ものである。
On the other hand, the styrene sulfonate as the other copolymerization component is not particularly limited, but alkali metal salts such as sodium salts and potassium salts are preferred.

かかる共重合体において、各共重合成分の構成比はとく
に限定されるものではないが、例えば、インブチレン 
1モルに対して、マレイン酸もしくはその無水物が0.
5〜5モル、スチレンスルホン酸塩0.01〜5モルと
なるようにそれぞれ設定されることが好ましい。また、
この共重合体の数平均分子量は500〜200,000
 、さらには、 1,000〜100.000であるこ
とが好ましい。
In such a copolymer, the composition ratio of each copolymer component is not particularly limited, but for example, inbutylene
0.1 mole of maleic acid or its anhydride.
It is preferable to set the amount to be 5 to 5 mol and the styrene sulfonate to 0.01 to 5 mol, respectively. Also,
The number average molecular weight of this copolymer is 500 to 200,000.
, and more preferably from 1,000 to 100,000.

この共重合体は、例えば次のようにして製造することが
できる。すなわち、まず、所定量のイソブチレン、無水
マレイン酸およびスチレンを所望により溶媒および触媒
の存在下で反応させることによりインブチレン−無水マ
レイン酸−スチレン共重合体を得る。このときの反応温
度は45〜150℃、反応時間は 1−10時間にそれ
ぞれ設定することが好ましい。なお、使用する溶媒とし
ては、アセトントリル、こトロメタン、ニトロエタン、
メチルエチルケトン、アセトン、N、N−ジメチルホル
ムアミド、ジメチルスルホキシドなどをあげることが〒
き、一方、触媒としては、ベンゾイルパーオキシド、ク
メンヒドロパーオキシド、第3級ブチルヒドロパーオキ
シド、過酸化ラウロイル、ジクミルパーオキシド、アゾ
ビスイソブチロニトリルなどがあげられる。
This copolymer can be produced, for example, as follows. That is, first, an inbutylene-maleic anhydride-styrene copolymer is obtained by reacting predetermined amounts of isobutylene, maleic anhydride, and styrene in the presence of a solvent and a catalyst if desired. At this time, the reaction temperature is preferably set at 45 to 150°C, and the reaction time is preferably set at 1 to 10 hours. The solvents used include acetontrile, tromethane, nitroethane,
Examples include methyl ethyl ketone, acetone, N,N-dimethylformamide, dimethyl sulfoxide, etc.
On the other hand, examples of the catalyst include benzoyl peroxide, cumene hydroperoxide, tertiary butyl hydroperoxide, lauroyl peroxide, dicumyl peroxide, and azobisisobutyronitrile.

ついで、該共重合体を通常の方法にてスルホン化し、共
重合成分であるスチレンをスチレンスルホン酸に転化せ
しめる。しかるのち、このものに、例えばライミングソ
ーデーションを行ないスルホン酸のナトリウム塩として
、目的とする本発明の共重合体を得る。
The copolymer is then sulfonated by a conventional method to convert the copolymer component styrene into styrene sulfonic acid. Thereafter, this product is subjected to, for example, liming sodation to obtain the desired copolymer of the present invention as a sodium salt of sulfonic acid.

なお、本発明の共重合体は、前述した製法のほかに、イ
ンブチレンと無水マレイン酸とスチレンスルホン酸塩と
を直接共重合させることにより製造することもできる。
In addition to the method described above, the copolymer of the present invention can also be produced by directly copolymerizing inbutylene, maleic anhydride, and styrene sulfonate.

[実施例] 実施例1〜3 (1)乳化重合用分散剤の製造 内容積11の回転式オートクレーブ中にインブチレン、
無水マレイン酸およびスチレンをそれぞれ第1表に示し
た使用量にて仕込み、さらに、触媒としてベンゾイルパ
ーオキシドO0θg、溶媒としてアセトニトリル460
−を仕込んだのち、 110°CC1400rpの条件
下2時間共重合反応させた。
[Examples] Examples 1 to 3 (1) Production of dispersant for emulsion polymerization In a rotary autoclave with an internal volume of 11, imbutylene,
Maleic anhydride and styrene were charged in the amounts shown in Table 1, and benzoyl peroxide O0θg was added as a catalyst, and acetonitrile 460g was added as a solvent.
After charging -, a copolymerization reaction was carried out for 2 hours at 110°C and 1400 rpm.

反応終了後、生成物を水中に投入してイソブチレン−無
水マレイン酸−スチレン共重合体を得た。
After the reaction was completed, the product was poured into water to obtain an isobutylene-maleic anhydride-styrene copolymer.

ついで、このものを粉砕したのち、それぞれ1(lag
を採取し、98%硫酸200gを加え、 100℃で2
時間反応させてスルホン化した。しかるのち、このもの
に水500gを加えて希釈し、80℃においてライミン
グソーデーションを行なうことによりナトリウム塩とし
た。得られた生成物を乾燥してイソブチレン−無水マレ
イン酸−スチレンスルホン酸塩共重合体よりなる本発明
の乳化重合用分散剤を得た。第1表には、イソブチレン
、無水マレイン酸およびスチレンの仕込み比(モル比)
および、最終的に得られた共重合体の数平均分子量を併
せて示した。
Next, after crushing this material, 1 (lag
200g of 98% sulfuric acid was added, and the mixture was heated at 100℃ for 2 hours.
Sulfonation was carried out by reaction for a period of time. Thereafter, this product was diluted with 500 g of water and subjected to liming sodation at 80°C to obtain a sodium salt. The obtained product was dried to obtain a dispersant for emulsion polymerization of the present invention comprising an isobutylene-maleic anhydride-styrene sulfonate copolymer. Table 1 shows the charging ratio (mole ratio) of isobutylene, maleic anhydride, and styrene.
The number average molecular weight of the finally obtained copolymer is also shown.

第1表 (2)ビニル系モノマーの乳化重合反応上記により得ら
れた乳化重合用分散剤を使用して、まず、酢酸ビニルの
乳化重合反応開始時の分散状態を評価した。すなわち、
反応媒体として水、重合開始剤として過硫酸カリウム、
界面活性剤としてラウリルベンゼンスルホン酸ナトリウ
ムを使用し、それぞれ表示の配合量(すべて重量部)で
使用した。まず、過硫酸カリウム、界面活性剤および分
散剤を水に溶解したのち、酢酸ビニルを加え、ラボディ
スパー (特殊機化工業■製)を使用して、室温下、1
000rp+sで2分間撹拌した。しかるのち、攪拌を
停止し、重合開始時の溶液中の分散状態を目視により観
察し、結果を表中に示した。
Table 1 (2) Emulsion polymerization reaction of vinyl monomers Using the dispersant for emulsion polymerization obtained above, first, the dispersion state at the start of the emulsion polymerization reaction of vinyl acetate was evaluated. That is,
Water as reaction medium, potassium persulfate as polymerization initiator,
Sodium laurylbenzenesulfonate was used as a surfactant, and each was used in the indicated amounts (all parts by weight). First, after dissolving potassium persulfate, a surfactant, and a dispersant in water, vinyl acetate was added, and using a lab body spar (manufactured by Tokushu Kika Kogyo ■), the mixture was heated for 1 hour at room temperature.
Stirred for 2 minutes at 000 rpm+s. Thereafter, the stirring was stopped, and the state of dispersion in the solution at the start of polymerization was visually observed, and the results are shown in the table.

ついで、同じく各成分を表示の配合量で使用することに
より酢酸ビニルの乳化重合反応を行なった。
Next, an emulsion polymerization reaction of vinyl acetate was carried out using each component in the indicated amounts.

すなわち、丸底四ツ目フラスコにラウリルベンゼンスル
ホン酸ナトリウムおよび分散剤を溶解せしめた水溶液を
調製し、攪拌しながら、温浴で加温して50℃まで昇温
した。つぎに、酢酸ビニルを滴下ロートから 1時間か
けて滴下した。一方で、過硫酸カリウムを10dの水に
溶解させ、この水溶液をフラスコ中に分割して添加した
。このとき、酢酸ビニルの滴下終了と同時に該過硫酸カ
リウム水溶液の添加が終了するようにした。その後、 
1時間重合反応を行なわせ酢酸ビニルの重合乳化物を得
た。この重合乳化物の乳化状態を目視により観察し、結
果を表中に示した。
That is, an aqueous solution in which sodium laurylbenzenesulfonate and a dispersant were dissolved was prepared in a round-bottomed four-eye flask, and heated in a hot bath to 50° C. while stirring. Next, vinyl acetate was added dropwise from the dropping funnel over a period of 1 hour. Meanwhile, potassium persulfate was dissolved in 10 d of water, and this aqueous solution was added in portions into the flask. At this time, the addition of the potassium persulfate aqueous solution was completed at the same time as the dropwise addition of vinyl acetate was completed. after that,
The polymerization reaction was carried out for 1 hour to obtain a polymerized emulsion of vinyl acetate. The emulsification state of this polymer emulsion was visually observed, and the results are shown in the table.

比較例1および2 乳化重合用分散剤として、下記に示す無水マレイン酸−
イソブチレン共重合体のNaOH中和物AおよびBを使
用したほかは、上記実施例1〜3と全く同様にして重合
開始時の分散状態および得られた重合乳化物の乳化状態
をそれぞれ目視により観察して結果を表中に併記した。
Comparative Examples 1 and 2 Maleic anhydride shown below was used as a dispersant for emulsion polymerization.
The dispersion state at the start of polymerization and the emulsification state of the obtained polymer emulsion were visually observed in exactly the same manner as in Examples 1 to 3 above, except that NaOH neutralized products A and B of isobutylene copolymer were used. The results are also listed in the table.

A:数平均分子量53,000、中和度1、無水マレイ
ン酸:イソブチレン= 1:0.8(モル比)B:数平
均分子量84,000、中和度l、無水マレイン酸:イ
ソブチレン= 1:0.8(モル比)[発明の効果] 以上の説明から明らかなように、本発明の乳化重合用分
散剤をビニル糸上ツマ−の乳化重合反応に使用した場合
、まず、重合反応開始時の分散性が良好であるとともに
、しかも、得られた重合乳化物の乳化状態が均一となる
ため、とくに、紙、木材用加工剤、接着剤および塗料な
どの原料として有用なビニル系ポリマーの製造分野にお
いて。
A: Number average molecular weight 53,000, degree of neutralization 1, maleic anhydride: isobutylene = 1:0.8 (mole ratio) B: number average molecular weight 84,000, degree of neutralization 1, maleic anhydride: isobutylene = 1 : 0.8 (mole ratio) [Effect of the invention] As is clear from the above explanation, when the dispersant for emulsion polymerization of the present invention is used in the emulsion polymerization reaction of vinyl thread yarn, first, the polymerization reaction starts. In addition, the resulting polymer emulsion has good dispersibility and a uniform emulsified state, making it particularly useful for vinyl polymers that are useful as raw materials for paper, wood processing agents, adhesives, paints, etc. In the manufacturing field.

その有用性は極めて高い。Its usefulness is extremely high.

Claims (1)

【特許請求の範囲】[Claims] イソブチレン−マレイン酸もしくはその無水物−スチレ
ンスルホン酸塩共重合体からなることを特徴とする乳化
重合用分散剤。
A dispersant for emulsion polymerization, characterized in that it consists of an isobutylene-maleic acid or anhydride-styrene sulfonate copolymer.
JP17407985A 1985-08-09 1985-08-09 Dispersing agent for emulsion polymerization Granted JPS6234901A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17407985A JPS6234901A (en) 1985-08-09 1985-08-09 Dispersing agent for emulsion polymerization

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17407985A JPS6234901A (en) 1985-08-09 1985-08-09 Dispersing agent for emulsion polymerization

Publications (2)

Publication Number Publication Date
JPS6234901A true JPS6234901A (en) 1987-02-14
JPH0130842B2 JPH0130842B2 (en) 1989-06-22

Family

ID=15972279

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17407985A Granted JPS6234901A (en) 1985-08-09 1985-08-09 Dispersing agent for emulsion polymerization

Country Status (1)

Country Link
JP (1) JPS6234901A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4789716A (en) * 1986-10-14 1988-12-06 Huls Aktiengesellschaft Method of manufacturing polymaleic anhydride powders

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4789716A (en) * 1986-10-14 1988-12-06 Huls Aktiengesellschaft Method of manufacturing polymaleic anhydride powders

Also Published As

Publication number Publication date
JPH0130842B2 (en) 1989-06-22

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