JPS6222802A - Dispersant for emulsion polymerization - Google Patents

Dispersant for emulsion polymerization

Info

Publication number
JPS6222802A
JPS6222802A JP16027085A JP16027085A JPS6222802A JP S6222802 A JPS6222802 A JP S6222802A JP 16027085 A JP16027085 A JP 16027085A JP 16027085 A JP16027085 A JP 16027085A JP S6222802 A JPS6222802 A JP S6222802A
Authority
JP
Japan
Prior art keywords
dispersant
anhydride
emulsion polymerization
maleic acid
copolymer
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
JP16027085A
Other languages
Japanese (ja)
Other versions
JPH0130841B2 (en
Inventor
Hidetoshi Shimada
英俊 島田
Jiro Yasumura
安村 二郎
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 JP16027085A priority Critical patent/JPS6222802A/en
Publication of JPS6222802A publication Critical patent/JPS6222802A/en
Publication of JPH0130841B2 publication Critical patent/JPH0130841B2/ja
Granted legal-status Critical Current

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  • Polymerisation Methods In General (AREA)

Abstract

PURPOSE:The titled dispersant which can improve the dispersibility of a vinyl monomer and give a polymer emulsion in a stable emulsified state, comprising a maleic acid (anhydride)/styrenesulfonate copolymer. CONSTITUTION:A maleic acid (anhydride)/styrene copolymer obtained by reacting 1mol of maleic acid (anhydride) with 1-5mol of styrene in the presence of a catalyst such as benzoyl peroxide or lauryl peroxide is sulfonated and then subjected to liming and sodation to obtain a dispersant for emulsion polymerization comprising a maleic acid (anhydride)/styrenesulfonate copolymer of a number-average MW of 500-200,000.

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、モノ
マー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 emulsion polymerization of vinyl monomers to improve the dispersibility of the monomers, The present invention also relates to a dispersant for emulsion polymerization that can produce a polymer emulsion in a 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七ツマ
−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 nanatsumer by adding it.

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、七ツマ−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 vinyl monomer described above, the dispersibility of the seven polymers in water is not very good, so the polymerization reaction cannot be carried out smoothly. There was a problem that the process did not proceed and furthermore, the stability of the obtained polymerized 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] 本発明者らは、上記目的を解消すべく鋭意研究を重ねた
結果、分散剤を構成する共重合体において、一方の共重
合成分として従来のイソブチ。
[Means for Solving the Problems] As a result of extensive research in order to solve the above object, the present inventors found that conventional isobutylene was used as one of the copolymer components in the copolymer constituting the dispersant.

レンに代えてスチレンスルホン酸塩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。
The present invention was completed by confirming that excellent effects can be obtained by using styrene sulfonate instead of styrene.

すなわち1本発明の乳化重合用分散剤は、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。
Specifically, the dispersant for emulsion polymerization of the present invention is characterized by comprising a maleic acid or anhydride-styrene sulfonate copolymer.

[A体内説明] 本発明の乳化重合用分散剤は、上述したように1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よ
りなる共重合体であり、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。
[In-body explanation A] As mentioned above, the dispersant for emulsion polymerization of the present invention is a copolymer consisting of monomaleic acid or its anhydride and styrene sulfonate, and this is particularly suitable for emulsification of vinyl monomers. It is useful for use in polymerization reactions.

まず、上述の共重合体において、第1の共重合成分はマ
レイン酸もしくはその無水物であるが、こノ他に、マレ
イン酸モノエステル、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。一方、第2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。
First, in the above copolymer, the first copolymerization component is maleic acid or its anhydride, but in addition to this, maleic acid monoester, maleic diester, maleic acid imide, or N-substituted maleic imide It is also possible to use maleic acid derivatives such as. On the other hand, the styrene sulfonate as the second copolymerization component is not particularly limited, but alkali metal salts such as sodium salts and potassium salts are preferred.

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、マレイン酸もしくはその無水物
とスチレンとを、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の触媒の存在下で反応させて、マレ
イン酸もしくはその無水物−スチレン共重合体を製造す
る。ついで、この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、例えばライイ
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。この工程
において、当初のマレイン酸もしくはその無水物とスチ
レンとの仕込み比はとくに限定されるものではないが、
例えば、マレイン酸もしくはその無水物1モルに対して
メチレフ1〜5モル程度となるように設定することが好
ましい。また、最終的に得られる共重合体の数平均分子
量は、 500〜200,000、さらには 1,00
0〜100,000であることが好ましい。なお、この
共重合体は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してもよい。
This copolymer can be produced, for example, as follows. That is, first, maleic acid or its anhydride and styrene are mixed with a catalyst such as benzoyl peroxide, cumene hydroperoxide, tertiary butyl hydroperoxide, lauroyl peroxide, dicumyl peroxide, azobisisobutyronitrile, etc. to produce a maleic acid or anhydride-styrene copolymer. This 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, lying sodation to obtain the desired copolymer of the present invention as a sodium salt of sulfonic acid. In this step, the initial charging ratio of maleic acid or its anhydride to styrene is not particularly limited;
For example, it is preferable to set the amount of methyl ref to about 1 to 5 moles per mole of maleic acid or its anhydride. Moreover, the number average molecular weight of the copolymer finally obtained is 500 to 200,000, and even 1,00.
It is preferably 0 to 100,000. Note that this copolymer may be produced by directly copolymerizing 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 スチレンおよび無水マレイン酸をそれぞれ第1表に示し
た使用量にて仕込み、触媒としてのペンンイルパーオキ
サイドの存在下 175℃で共重合させてマレイン酸−
スチレン共重合体を得た。ついで、この重合体100g
に対して98%硫酸200gを加え、 100℃で2時
間反応させてスルホン化した。
[Examples] Examples 1 to 3 (1) Production of dispersant for emulsion polymerization Styrene and maleic anhydride were charged in the amounts shown in Table 1, and in the presence of penyl peroxide as a catalyst. Maleic acid was copolymerized at ℃.
A styrene copolymer was obtained. Then, 100g of this polymer
200 g of 98% sulfuric acid was added thereto, and the mixture was reacted at 100°C for 2 hours to effect sulfonation.

しかるのち、このものに水を500gを加えて希釈し、
60°Cにおいてライイ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、無
水マレイン酸に対する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。
After that, add 500g of water to dilute this,
The sodium salt was obtained by carrying out lying sodation at 60°C. The obtained product was dried to obtain a dispersant for emulsion polymerization of the present invention comprising a maleic anhydride-styrene sulfonate copolymer. Table 1 also shows the charging ratio (mole ratio) of styrene to maleic anhydride and the number average molecular weight of the finally obtained copolymer.

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、 
1000rpa+で2分間攪拌した。しかるのち、攪拌
を停止し1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 solution was dissolved at room temperature.
Stirred for 2 minutes at 1000 rpa+. Thereafter, stirring was stopped, and the dispersion state in the solution at the start of 1st 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、丸底四ツロ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、湯浴で加温して50℃まで昇温
した。つぎに、酢酸ビニルを滴下ロートから 14間か
けて滴下した。一方で、過硫酸カリウムをlO−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、2
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 four-bottomed round-bottomed flask, and heated to 50° C. in a hot water bath while stirring. Next, vinyl acetate was added dropwise from the dropping funnel over a period of 14 hours. Meanwhile, potassium persulfate was dissolved in lO- 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, 2
A time polymerization reaction was carried out to obtain a polymer 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 Polymerization was carried out in exactly the same manner as in Examples 1 to 3 above, except that NaOH neutralized products A and B of the maleic anhydride-isobutylene copolymer shown below were used as the dispersant for emulsion polymerization. The dispersion state at the beginning and the emulsification state of the obtained polymer emulsion were visually observed, and the results are also shown in the table.

A:数平均分子[53,000、中和度1、無水マレイ
ン酸:イソブチル= 1:1(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
チル=に巨モル比) [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、その有用性は極めて高い。
A: Number average molecular weight [53,000, degree of neutralization 1, maleic anhydride: isobutyl = 1:1 (molar ratio) B: number average molecular weight 84,000, degree of neutralization 1, maleic anhydride: isobutyl = [Effects 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 yarn yarn, first, the dispersibility at the start of the polymerization reaction improves. In addition, the obtained polymer emulsion has a uniform emulsification state, so it is particularly useful in the field of producing vinyl polymers useful as raw materials for paper, wood processing agents, adhesives, paints, etc. Its usefulness is extremely high.

Claims (1)

【特許請求の範囲】[Claims] 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 by comprising a maleic acid or its anhydride-styrene sulfonate copolymer.
JP16027085A 1985-07-22 1985-07-22 Dispersant for emulsion polymerization Granted JPS6222802A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16027085A JPS6222802A (en) 1985-07-22 1985-07-22 Dispersant for emulsion polymerization

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16027085A JPS6222802A (en) 1985-07-22 1985-07-22 Dispersant for emulsion polymerization

Publications (2)

Publication Number Publication Date
JPS6222802A true JPS6222802A (en) 1987-01-31
JPH0130841B2 JPH0130841B2 (en) 1989-06-22

Family

ID=15711367

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16027085A Granted JPS6222802A (en) 1985-07-22 1985-07-22 Dispersant for emulsion polymerization

Country Status (1)

Country Link
JP (1) JPS6222802A (en)

Also Published As

Publication number Publication date
JPH0130841B2 (en) 1989-06-22

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