JP3197353B2 - Method for producing degradable polymer dispersion - Google Patents

Method for producing degradable polymer dispersion

Info

Publication number
JP3197353B2
JP3197353B2 JP22287992A JP22287992A JP3197353B2 JP 3197353 B2 JP3197353 B2 JP 3197353B2 JP 22287992 A JP22287992 A JP 22287992A JP 22287992 A JP22287992 A JP 22287992A JP 3197353 B2 JP3197353 B2 JP 3197353B2
Authority
JP
Japan
Prior art keywords
polymer
methylstyrene
plasticizer
polymer dispersion
degradable polymer
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
JP22287992A
Other languages
Japanese (ja)
Other versions
JPH0665385A (en
Inventor
浅沼  正
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.)
Mitsui Chemicals Inc
Original Assignee
Mitsui Chemicals Inc
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 Mitsui Chemicals Inc filed Critical Mitsui Chemicals Inc
Priority to JP22287992A priority Critical patent/JP3197353B2/en
Publication of JPH0665385A publication Critical patent/JPH0665385A/en
Application granted granted Critical
Publication of JP3197353B2 publication Critical patent/JP3197353B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は分解性のポリマー分散液
を製造する方法に関する。詳しくは特定の高分子化合物
と可塑剤を加熱下に混合して分散液を製造する方法に関
する。
FIELD OF THE INVENTION The present invention relates to a method for producing a degradable polymer dispersion. More specifically, the present invention relates to a method for producing a dispersion by mixing a specific polymer compound and a plasticizer while heating.

【0002】[0002]

【従来の技術】分解性のポリマーをバインダーとして用
いたり、あるいは分解性の膜を製造したりさらには分解
性の接着剤として用いることは広く行われており、通常
分解性のポリマーは溶剤に溶解した状態で用いることが
行われている。溶剤としては分解性のポリマーは通常水
には溶解しないので有機溶剤に溶解して用いられてい
る。
2. Description of the Related Art The use of degradable polymers as binders, the production of degradable films, and the use of degradable adhesives are widely performed. Usually, degradable polymers are dissolved in solvents. It is used in the state where it was done. As a solvent, a decomposable polymer is not dissolved in water, and is used by dissolving it in an organic solvent.

【0003】[0003]

【発明が解決しようとする課題】しかし分解性のポリマ
ー溶液は使用に際し有機溶剤は蒸発除去されるため、溶
剤の無害化とか回収の必要があり、場合によっては利用
する設備を防爆設備にする必要があるなどの問題があ
る。
However, since the organic solvent of the decomposable polymer solution is removed by evaporation during use, it is necessary to make the solvent harmless or to recover it. In some cases, it is necessary to use explosion-proof equipment. There are problems such as.

【0004】[0004]

【課題を解決するための手段】本発明者らは上記問題を
解決して、有機溶剤を使用しない分解性の分散液の製造
方法について鋭意探索し本発明を完成した。
Means for Solving the Problems The present inventors have solved the above problems, and have intensively searched for a method for producing a degradable dispersion liquid without using an organic solvent, and have completed the present invention.

【0005】即ち本発明は、ポリα−メチルスチレンあ
るいはポリアルキレンカーボネートと、可塑剤を、ポリ
α−メチルスチレンあるいはポリアルキレンカーボネー
トと可塑剤の混合物が可塑化する温度以上の温度の加熱
下に水中に分散させることを特徴とする分解性ポリマー
分散液の製造方法である。
That is, the present invention relates to a method for preparing a poly-α-methylstyrene or polyalkylene carbonate ,
α-methylstyrene or polyalkylene carbonate
A method for producing a degradable polymer dispersion, comprising dispersing in water under heating at a temperature not lower than the temperature at which the mixture of the polymer and the plasticizer is plasticized .

【0006】本発明において、ポリα−メチルスチレン
としてはα−メチルスチレンをアニオン重合することで
得られる高分子量の重合体が用いられ、分解性を損なわ
ない範囲で他のスチレン系のモノマーを共重合したも
の、例えば、スチレンを用いる場合では50モル%以下、
が用いられ、数平均分子量としては5000〜1000000 程
度、好ましくは10000 〜500000程度のものが利用され
る。またポリアルキレンカーボネートとしては、触媒を
用いて炭素数2 〜10のアルキレンオキサイドと二酸化炭
素を共重合して得られるものが挙げられ、分子量として
は、1000〜1000000 、通常5000〜500000程度のものが利
用できる。
In the present invention, a high molecular weight polymer obtained by anionic polymerization of α-methylstyrene is used as polyα-methylstyrene, and other polystyrene-based monomers are used as long as the decomposability is not impaired. Polymerized, for example, when styrene is used, 50 mol% or less,
And a number average molecular weight of about 5,000 to 100,000, preferably about 10,000 to 500,000. Examples of the polyalkylene carbonate include those obtained by copolymerizing an alkylene oxide having 2 to 10 carbon atoms and carbon dioxide using a catalyst, and having a molecular weight of 1,000 to 100,000, usually about 5,000 to 500,000. Available.

【0007】本発明においては上記ポリマーは可塑剤と
混合して用いられる。ここで可塑剤としては、融点の低
い、比較的沸点の高い化合物が利用され、フタル酸のエ
ステル、燐酸のエステル、α−メチルスチレンのオリゴ
マーなどが利用される。上記ポリマーと可塑剤の使用割
合としてはポリマー100 に対して200 〜1程度であるの
が一般的である。
In the present invention, the above-mentioned polymer is used by mixing with a plasticizer. Here, as the plasticizer, a compound having a low melting point and a relatively high boiling point is used, and an ester of phthalic acid, an ester of phosphoric acid, and an oligomer of α-methylstyrene are used. The usage ratio of the polymer and the plasticizer is generally about 200 to 1 per 100 of the polymer.

【0008】こうして可塑剤との混合を水との混合に先
立って行うことも可能であるが充分に混合が可能な装置
を用いるのであれば、水と混合すると同時に行っても良
い。水と混合する際には、少量の界面活性剤、水溶性の
ポリマーを存在させるのが好ましい。ここで界面活性剤
の使用量としては、水100 に対して0.01〜5、通常0.1
〜2 程度であり、上記ポリマーと可塑剤の総和は1〜10
0 、特に5〜50程度である。混合に際しては加熱するこ
とが肝要であり加熱温度としては、ポリマーと可塑剤の
混合物が可塑化する温度以上であり、必要に応じ加圧下
に行われる。通常50〜300 ℃で行うのが一般的である。
この際に、水性エマルジョンを安定化するため水酸化ナ
トリウム、水酸化カリウム、水酸化カルシウム、リン酸
ナトリウム、リン酸二水素ナトリウム、リン酸カリウ
ム、リン酸二水素カリウムなどを用いることも可能であ
る。界面活性剤としては、ノニオン系、アニオン系の界
面活性剤が利用でき種々のものが市場で入手可能であり
具体的にはアルキルベンゼンスルホン酸ソーダ、アルキ
ルスルホン酸ソーダ、ポリエチレンオキサイドアルキル
エーテル、ポリエチレンオキサイドアルキルベンゼンエ
ーテルなどが例示される。分散液とするためには混合は
強攪拌下に行うのが好ましく、そのような装置としてす
でに種々のものが知られており、市場で入手することが
できる。
Thus, the mixing with the plasticizer can be performed prior to the mixing with the water, but if a device capable of sufficiently mixing is used, the mixing with the water may be performed at the same time. When mixing with water, a small amount of a surfactant and a water-soluble polymer are preferably present. Here, the amount of the surfactant used is 0.01 to 5, usually 0.1
About 2 and the total of the polymer and the plasticizer is 1 to 10
0, especially about 5 to 50. Heating is essential for mixing, and the heating temperature is equal to or higher than the temperature at which the mixture of the polymer and the plasticizer is plasticized, and is performed under pressure as necessary. Usually, it is carried out at 50 to 300 ° C.
At this time, it is also possible to use sodium hydroxide, potassium hydroxide, calcium hydroxide, sodium phosphate, sodium dihydrogen phosphate, potassium phosphate, potassium dihydrogen phosphate or the like to stabilize the aqueous emulsion. . As the surfactant, nonionic and anionic surfactants can be used, and various surfactants are available on the market. Specifically, sodium alkylbenzene sulfonate, sodium alkyl sulfonate, polyethylene oxide alkyl ether, polyethylene oxide alkylbenzene Ether is exemplified. In order to obtain a dispersion, the mixing is preferably performed under strong stirring, and various types of such devices are already known and can be obtained on the market.

【0009】[0009]

【実施例】以下に実施例を示しさらに本発明を説明す
る。
The present invention will be further described with reference to examples.

【0010】実施例1 α−メチルスチレンをブチルリチウムを用いて重合して
得た、数平均分子量120000のポリα−メチルスチレン12
g とα−メチルスチレンの3量体8g をドデシルベンゼ
ンスルホン酸ソーダ1g を水100ml に溶解したものに加
え150 ℃でオートクレーブを用い良く攪拌した。攪拌し
ながら30℃まで降温した後分散液を取り出したところ均
一に分散した液が得られた。この分散液をガラス板に塗
布し、乾燥して厚さ3μm の膜を形成した。この膜を38
0 ℃で1時間処理したところ、完全に塗膜は飛散した。
Example 1 Poly-α-methylstyrene 12 having a number average molecular weight of 120,000 was obtained by polymerizing α-methylstyrene using butyllithium.
g and 8 g of a trimer of α-methylstyrene were added to a solution of 1 g of sodium dodecylbenzenesulfonate in 100 ml of water, and the mixture was stirred well at 150 ° C. using an autoclave. After the temperature was lowered to 30 ° C. with stirring, the dispersion was taken out to obtain a uniformly dispersed liquid. This dispersion was applied to a glass plate and dried to form a film having a thickness of 3 μm. 38
When treated at 0 ° C. for 1 hour, the coating film was completely scattered.

【0011】実施例2 プロピレンオキサイドと二酸化炭素を重合して得たポリ
プロピレンカーボネート(分子量8万)を水酸化ナトリ
ウム水溶液で加水分解して得たオリゴマー(分子量約45
00)20g とフタル酸ジオクチル2g を用いた他は実施例
1と同様にしたところ、同様に均一な分散液が得られ、
その液を塗布することで均一な膜が得られた。
Example 2 An oligomer (molecular weight of about 45) obtained by hydrolyzing polypropylene carbonate (molecular weight: 80,000) obtained by polymerizing propylene oxide and carbon dioxide with an aqueous sodium hydroxide solution.
00) Except that 20 g and 2 g of dioctyl phthalate were used, the same procedure was performed as in Example 1 to obtain a homogeneous dispersion.
A uniform film was obtained by applying the liquid.

【0012】[0012]

【発明の効果】本発明の方法を実施することにより分解
性のポリマーの水性分散液が得られ工業的に極めて価値
がある。
By carrying out the method of the present invention, an aqueous dispersion of a degradable polymer is obtained, which is extremely valuable industrially.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】ポリα−メチルスチレンあるいはポリアル
キレンカーボネートと、可塑剤を、ポリα−メチルスチ
レンあるいはポリアルキレンカーボネートと可塑剤の混
合物が可塑化する温度以上の温度の加熱下に水中に分散
させることを特徴とする分解性ポリマー分散液の製造方
法。
1. A poly-α-methylstyrene or polyalkylene carbonate and a plasticizer are mixed with poly-α-methylstyrene.
Mixture of plasticizer and ren or polyalkylene carbonate
A method for producing a degradable polymer dispersion, comprising dispersing in water under heating at a temperature not lower than the temperature at which the compound is plasticized .
JP22287992A 1992-08-21 1992-08-21 Method for producing degradable polymer dispersion Expired - Fee Related JP3197353B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22287992A JP3197353B2 (en) 1992-08-21 1992-08-21 Method for producing degradable polymer dispersion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22287992A JP3197353B2 (en) 1992-08-21 1992-08-21 Method for producing degradable polymer dispersion

Publications (2)

Publication Number Publication Date
JPH0665385A JPH0665385A (en) 1994-03-08
JP3197353B2 true JP3197353B2 (en) 2001-08-13

Family

ID=16789320

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22287992A Expired - Fee Related JP3197353B2 (en) 1992-08-21 1992-08-21 Method for producing degradable polymer dispersion

Country Status (1)

Country Link
JP (1) JP3197353B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1156741C (en) 1998-04-16 2004-07-07 国际商业机器公司 Chinese handwriting identifying method and device

Also Published As

Publication number Publication date
JPH0665385A (en) 1994-03-08

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