JPH0576485B2 - - Google Patents
Info
- Publication number
- JPH0576485B2 JPH0576485B2 JP59106471A JP10647184A JPH0576485B2 JP H0576485 B2 JPH0576485 B2 JP H0576485B2 JP 59106471 A JP59106471 A JP 59106471A JP 10647184 A JP10647184 A JP 10647184A JP H0576485 B2 JPH0576485 B2 JP H0576485B2
- Authority
- JP
- Japan
- Prior art keywords
- polymerization
- water
- polymer
- formula
- methyl group
- 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 - Lifetime
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
産業上の利用分野:
本発明は水性組成物に関する。更に詳しくは特
定の単量体を特定状態で重合してなる重合体と水
よりなり、曇点の上下でその状態が変化する水性
組成物に関する。
従来技術とその問題点:
従来、水溶性重合体は増粘剤、高分子凝集剤等
の分野で水性ペーストとして使用されており、そ
の際水溶性重合体の分子量が高ければ高い程添加
量が少くて済み好都合である。しかし、分子量を
高くすると、その水溶液の粘度が極めて高くなつ
てしまい、実際に重合体を水溶性の状態で製造す
るにはその点が大きな問題点となつてしまう。
一方、エマルシヨン重合の1つの大きな特徴と
して、重合体の分子量を極めて大きくできる点が
あり、その特徴を生かした重合技術の開発も行わ
れているが、水溶性重合体の製造への応用は見い
出されていない。
問題点を解決するための手段:
本発明者らは上記した点に鑑みエマルシヨン重
合技術の水溶性重合体製造への応用について鋭意
検討した結果、特定のアクリルアミドまたはメタ
アクリルアミド誘導体(以下、(メタ)アクリル
アミド誘導体と略記する。)を用い特定状態で重
合することにより感温性であり且つ高分子量の水
溶性重合体を含有してなる水性組成物が得られる
ことを見い出して本発明に到達した。
即ち、本発明は、一般式()または一般式
()
一般式
INDUSTRIAL FIELD OF APPLICATION: The present invention relates to aqueous compositions. More specifically, the present invention relates to an aqueous composition that is composed of a polymer obtained by polymerizing specific monomers in a specific state and water, and whose state changes above and below the cloud point. Conventional technology and its problems: Conventionally, water-soluble polymers have been used as water-based pastes in the fields of thickeners, polymer flocculants, etc. In this case, the higher the molecular weight of the water-soluble polymer, the higher the amount added. It is convenient because it is small. However, when the molecular weight is increased, the viscosity of the aqueous solution becomes extremely high, which poses a major problem in actually producing the polymer in a water-soluble state. On the other hand, one major feature of emulsion polymerization is that the molecular weight of the polymer can be extremely increased, and although polymerization technologies that take advantage of this feature are being developed, application to the production of water-soluble polymers has yet to be found. Not yet. Means for Solving the Problems: In view of the above points, the present inventors have conducted extensive studies on the application of emulsion polymerization technology to the production of water-soluble polymers. The present invention was achieved by discovering that an aqueous composition containing a temperature-sensitive, high-molecular-weight water-soluble polymer can be obtained by polymerizing acrylamide derivatives (abbreviated as acrylamide derivatives) in a specific state. That is, the present invention provides general formula () or general formula () general formula
【式】
(上式でR1は水素原子またはメチル基、R2は水
素原子、メチル基またはエチル基、R3はメチル
基またはエチル基を表わす。)
一般式[Formula] (In the above formula, R 1 represents a hydrogen atom or a methyl group, R 2 represents a hydrogen atom, a methyl group or an ethyl group, and R 3 represents a methyl group or an ethyl group.) General formula
参考例
表1に示す単量体または単量体混合物を使用し
て溶液重合を行い、重合後溶媒を除去して重合体
を得た。該重合体の濃度が10重量%となるように
蒸留水に溶解して、該水溶液を内径15mmの試験管
に入れ、そこに標準温度計を差し込み、恒温水中
で温度計で水溶液を撹拌しながら、徐々に加温し
た。水溶液が白濁し温度計の水銀球が見えなくな
る温度を白濁温度、即ち曇点として表1に示し
た。
Reference Example Solution polymerization was performed using the monomers or monomer mixtures shown in Table 1, and the solvent was removed after polymerization to obtain a polymer. Dissolve the polymer in distilled water to a concentration of 10% by weight, put the aqueous solution into a test tube with an inner diameter of 15 mm, insert a standard thermometer into it, and stir the aqueous solution with the thermometer in constant temperature water. , gradually warmed up. The temperature at which the aqueous solution becomes cloudy and the mercury bulb of the thermometer becomes invisible is shown in Table 1 as the cloudy temperature, that is, the cloud point.
【表】
実施例 1
水58.3gにN−アクリロイルピロリジン11.6g
及び2−アクリルアミド−2−フエニルプロパン
スルホン酸ナトリウム(以下APPS−Naと略
す。)0.47gを添加し、反応器内を窒素ガスで置
換した後、70℃に加温した。ついで該反応液に濃
度7%の過硫酸カリウム水溶液を1ml添加し重合
を開始し、7時間重合した。重合の進行に伴い重
合液は白濁し、その後は乳化した状態で進行し、
十分撹拌できた。得られた重合液を冷却したとこ
ろ、該重合液は透明となり、撹拌不能となつた。
そこで該重合液を蒸留水で濃度10%に稀釈して粘
度を測定したところ、25℃で117cpsであつた。
なお予めこの重合体のモノマー組成と同じ組成
の重合体について参考例と同様にして曇点を測定
した結果は51℃であつた。
比較例 1
100mlの4ツ口丸底フラスコに窒素ガス流通下
で撹拌しながら、蒸留水45.0g、N−アクリロイ
ルピロリジン5.0gを添加した。その後、過硫酸
アンモニウム0.5g及び亜硫酸水素ナトリウム
0.23gを添加し、15〜30℃で4時間重合し、N−
アクリロイルピロリジンの重合体の10%水溶液を
得た。該水溶液の粘度を測定したところ、25℃で
3.5cpsであつた。
実施例 2
水166gにN−アクリロイルピロリジン4.0g及
びAPPS−Na0.2gを添加し、反応器内を窒素ガ
スで置換した後、60℃に加温した。ついで該反応
液に過硫酸カリウム0.12gを添加して重合を開始
し、40分重合した。重合の進行に伴い重合液は白
濁し、その後は乳化した状態で進行した。つい
で、重合温度はそのままにしておき、水20gにN
−アクリロイルピロリジン9.9g、アクリル酸
0.14g及びAPPS−Na0.2gを添加溶解した水溶
液を1時間にわたつてポンプで添加した。その
後、更に6時間重合を行つた。得られた重合液の
粘度を測定したところ、50℃では23cps、25℃で
は5900cps、10℃では16000cpsであつた。なお、
その時重合液は50℃では乳化状態であり、25℃及
び10℃では透明であつた。さらに上記の重合液の
粘度測定を繰り返したところ、50℃では23cps、
25℃では5900cps、10℃では16000cpsであつた。
なお予めこの重合体のモノマー組成と同じ組成の
重合体について参考例と同様にして曇点を測定し
た結果は50℃であつた。
実施例 3
水500gにN−アクリロイルピペリジン15g及
びAPPS−Na1gを添加し、反応器内を窒素ガス
置換した後、50℃に加温した。ついで該反応液に
過硫酸カリウム0.5gを添加して重合を開始し、
1時間重合した。重合の進行に伴い重合液は白濁
し、その後は乳化した状態で進行した。ついで重
合温度はそのままにしておき、水100gにN−ア
クリロイルピペリジン35g及びAPPS−Na0.5g
を添加溶解した水溶液を1時間にわたつてポンプ
で添加した。その後更に6時間重合を行つた。得
られた重合液の粘度を測定したところ、10℃では
2.4cps、5℃では4.4cps、2℃では12.5cpsであつ
た。なお重合液は7℃では乳化状態であり、0℃
では透明であつた。
なお予めこの重合体のモノマー組成と同じ組成
の重合体について参考例と同様にして曇点を測定
した結果は6℃であつた。
実施例 4
水514gにN−アクリロイルピペリジン20g及
びAPPS−Na1.0gを添加し、反応器内を窒素ガ
スで置換した後、50℃に加温した。ついで該反応
液に過硫酸カリウム0.5gを添加して重合を開始
し、1時間重合した。重合の進行に伴い重合液は
白濁し、その後は乳化した状態で進行した。つい
で重合温度を40℃に下げて水150gにN−アクリ
ロイルピペリジン25g、N−メチロールメタクリ
ルアミド5.0g及びAPPS−Na0.5gを添加溶解し
た水溶液を1時間にわたつてポンプで添加した。
その後50℃に昇温して更に6時間重合を行つた。
得られた重合液の粘度を測定したところ、10℃で
は2.7cps、5℃では4.3cps、2℃では13.9cpsであ
つた。なお重合液は10℃及び5℃では乳化状態で
あり、0℃で透明になつた。なお予めこの重合体
のモノマー組成と同じ組成の重合体について参考
例と同様にして曇点を測定した結果は5℃であつ
た。[Table] Example 1 11.6 g of N-acryloylpyrrolidine in 58.3 g of water
and 0.47 g of sodium 2-acrylamido-2-phenylpropanesulfonate (hereinafter abbreviated as APPS-Na) were added, the inside of the reactor was purged with nitrogen gas, and then heated to 70°C. Next, 1 ml of an aqueous potassium persulfate solution having a concentration of 7% was added to the reaction solution to initiate polymerization, and the polymerization was continued for 7 hours. As the polymerization progresses, the polymerization solution becomes cloudy and then progresses in an emulsified state.
Sufficient stirring was possible. When the obtained polymerization liquid was cooled, it became transparent and could no longer be stirred.
Therefore, when the polymerization solution was diluted with distilled water to a concentration of 10% and the viscosity was measured, it was found to be 117 cps at 25°C. Note that the cloud point of a polymer having the same monomer composition as this polymer was previously measured in the same manner as in the reference example, and the result was 51°C. Comparative Example 1 45.0 g of distilled water and 5.0 g of N-acryloylpyrrolidine were added to a 100 ml four-necked round-bottomed flask while stirring under nitrogen gas flow. Then 0.5 g of ammonium persulfate and sodium bisulfite
Add 0.23g of N-
A 10% aqueous solution of acryloylpyrrolidine polymer was obtained. When the viscosity of the aqueous solution was measured, it was found that at 25℃
It was 3.5cps. Example 2 4.0 g of N-acryloylpyrrolidine and 0.2 g of APPS-Na were added to 166 g of water, the inside of the reactor was purged with nitrogen gas, and then heated to 60°C. Next, 0.12 g of potassium persulfate was added to the reaction solution to initiate polymerization, and the polymerization was continued for 40 minutes. As the polymerization progressed, the polymerization solution became cloudy, and thereafter proceeded in an emulsified state. Next, leave the polymerization temperature as it is and add N to 20g of water.
-Acryloylpyrrolidine 9.9g, acrylic acid
An aqueous solution containing 0.14 g and 0.2 g of APPS-Na was added by pump over 1 hour. Thereafter, polymerization was further carried out for 6 hours. When the viscosity of the obtained polymerization liquid was measured, it was 23 cps at 50°C, 5900 cps at 25°C, and 16000 cps at 10°C. In addition,
At that time, the polymerization solution was in an emulsified state at 50°C and transparent at 25°C and 10°C. Furthermore, when we repeated the viscosity measurement of the above polymerization solution, we found that it was 23 cps at 50°C.
At 25℃ it was 5900cps and at 10℃ it was 16000cps.
Note that the cloud point of a polymer having the same monomer composition as this polymer was previously measured in the same manner as in the reference example, and the result was 50°C. Example 3 15 g of N-acryloylpiperidine and 1 g of APPS-Na were added to 500 g of water, the inside of the reactor was purged with nitrogen gas, and then heated to 50°C. Then, 0.5 g of potassium persulfate was added to the reaction solution to start polymerization.
Polymerization was carried out for 1 hour. As the polymerization progressed, the polymerization solution became cloudy, and thereafter proceeded in an emulsified state. Next, while leaving the polymerization temperature as it is, add 35 g of N-acryloylpiperidine and 0.5 g of APPS-Na to 100 g of water.
The aqueous solution was added by pump over a period of 1 hour. Thereafter, polymerization was further carried out for 6 hours. When the viscosity of the obtained polymerization liquid was measured, it was found that at 10℃
It was 2.4cps, 4.4cps at 5℃, and 12.5cps at 2℃. The polymerization solution is in an emulsified state at 7°C, and at 0°C
It was transparent. Note that the cloud point of a polymer having the same monomer composition as this polymer was previously measured in the same manner as in the reference example, and the result was 6°C. Example 4 20 g of N-acryloylpiperidine and 1.0 g of APPS-Na were added to 514 g of water, the inside of the reactor was purged with nitrogen gas, and then heated to 50°C. Next, 0.5 g of potassium persulfate was added to the reaction solution to initiate polymerization, and the polymerization was continued for 1 hour. As the polymerization progressed, the polymerization solution became cloudy, and thereafter proceeded in an emulsified state. Then, the polymerization temperature was lowered to 40 DEG C., and an aqueous solution of 25 g of N-acryloylpiperidine, 5.0 g of N-methylolmethacrylamide, and 0.5 g of APPS-Na in 150 g of water was added over 1 hour using a pump.
Thereafter, the temperature was raised to 50°C and polymerization was continued for an additional 6 hours.
When the viscosity of the obtained polymerization liquid was measured, it was 2.7 cps at 10°C, 4.3 cps at 5°C, and 13.9 cps at 2°C. The polymerization solution was in an emulsified state at 10°C and 5°C, and became transparent at 0°C. Note that the cloud point of a polymer having the same monomer composition as this polymer was previously measured in the same manner as in the reference example, and the result was 5°C.
Claims (1)
る 【式】 (上式でR1は水素原子またはメチル基、R2は水
素原子、メチル基またはエチル基、R3はメチル
基、エチル基またはプロピル基を表す。) 【式】 (上式でR1は水素原子またはメチル基、Aは(―
OH2)o――でnは4〜6をまたは(―OH2)2――O(
―
OH2)2――を表す。) N−アルキルまたはN−アルキレン置換(メ
タ)アクリルアミドをエマルシヨン状態でラジカ
ル単独または共重合体せしめるか、もしくは他の
共重合しうる単量体とエマルシヨン状態でラジカ
ル共重合体せしめることを特徴とする曇点より下
の温度では水溶性であり、曇点以上の温度ではエ
マルシヨン状態となる重合体5〜60%、水95〜40
%とからなる水性組成物の製造方法。[Claims] 1 [Formula] represented by general formula () or general formula () (In the above formula, R 1 is a hydrogen atom or a methyl group, R 2 is a hydrogen atom, a methyl group or an ethyl group, and R 3 is (Represents a methyl group, ethyl group or propyl group.) [Formula] (In the above formula, R 1 is a hydrogen atom or a methyl group, and A is (-
OH 2 ) o -- and n is 4 to 6 or (-OH 2 ) 2 --O(
―
OH 2 ) 2 -- represents. ) N-alkyl- or N-alkylene-substituted (meth)acrylamide is formed into a radical homopolymer or a copolymer in an emulsion state, or a radical copolymer is formed with another copolymerizable monomer in an emulsion state. 5-60% polymer, 95-40% water, which is soluble in water at temperatures below the cloud point and forms an emulsion at temperatures above the cloud point.
%.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10647184A JPS61210A (en) | 1984-05-28 | 1984-05-28 | Polymer emulsion |
| EP85303161A EP0161104A3 (en) | 1984-05-07 | 1985-05-03 | Polymer emulsions and process of preparing polymer emulsions |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10647184A JPS61210A (en) | 1984-05-28 | 1984-05-28 | Polymer emulsion |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18738385A Division JPS6187717A (en) | 1985-08-28 | 1985-08-28 | Polymer emulsion |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61210A JPS61210A (en) | 1986-01-06 |
| JPH0576485B2 true JPH0576485B2 (en) | 1993-10-22 |
Family
ID=14434438
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10647184A Granted JPS61210A (en) | 1984-05-07 | 1984-05-28 | Polymer emulsion |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61210A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5835548B2 (en) * | 1976-03-24 | 1983-08-03 | 株式会社興人 | emulsion adhesive |
-
1984
- 1984-05-28 JP JP10647184A patent/JPS61210A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61210A (en) | 1986-01-06 |
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