Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0324254B2 - - Google Patents
[go: Go Back, main page]

JPH0324254B2 - - Google Patents

Info

Publication number
JPH0324254B2
JPH0324254B2 JP56112576A JP11257681A JPH0324254B2 JP H0324254 B2 JPH0324254 B2 JP H0324254B2 JP 56112576 A JP56112576 A JP 56112576A JP 11257681 A JP11257681 A JP 11257681A JP H0324254 B2 JPH0324254 B2 JP H0324254B2
Authority
JP
Japan
Prior art keywords
mol
vinyl monomer
monomer
viscosity
centipoise
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
Application number
JP56112576A
Other languages
Japanese (ja)
Other versions
JPS5813608A (en
Inventor
Rikio Tsushima
Yoshinao Kono
Yasuo Ishii
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.)
Kao Corp
Original Assignee
Kao Corp
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 Kao Corp filed Critical Kao Corp
Priority to JP56112576A priority Critical patent/JPS5813608A/en
Publication of JPS5813608A publication Critical patent/JPS5813608A/en
Publication of JPH0324254B2 publication Critical patent/JPH0324254B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は架橋両性共重合体からなる分散剤に関
する。更に詳しくは、香粧品、化粧品、医薬品、
乳化物、懸濁物等の調製に用いられる増粘・分散
剤、特に顔料、乳濁剤、水不溶性殺菌剤、パール
化剤、研磨剤等の水不溶性固体微粒子を安定に分
散しうる架橋両性共重合体からなる分散剤に関す
る。 従来、増粘・分散剤として各種の高分子電解質
が提案されているが、必ずしも満足すべきものが
得られていない。例えば、ポリアクリル酸架橋物
はその代表的なものであるが、これを増粘・分散
剤として用いた場合、系が酸性であつたり、可溶
性塩類が共存すると著るしく粘度が低下し、分散
能も低下する。他方、広いPH範囲で有効な分散剤
を得る試みとして特公昭54−3783号公報は両性共
重合体(未架橋)を提案する。しかしながら、そ
こに示されている両性共重合体も可溶性塩類の存
在する系においては必ずしも十分満足のゆくもの
ではなかつた。 そこで本発明者らは、広いPH範囲においても、
可溶性塩類が共存する系においても、優れた増粘
効果及び分散効果を発揮する高分子電解質を得る
べく鋭意研究した結果、酸性ビニル単量体又はそ
の塩45〜55モル%、塩基性ビニル単量体又はその
塩45〜55モル%及び架橋性単量体0.05〜1モル%
からなる混合単量体を、ラジカル重合開始剤の存
在下で20〜120℃の温度範囲で共重合することに
より、系のPH、可溶性塩類の有無に拘らず、水不
溶性固体微粒子物質を安定に分散させうる架橋両
性共重合体を製造しうることを見出し本発明を完
成した。 本発明に係る酸性ビニル単量体とは、1分子中
にカルボキシル基、スルホン酸基などの酸性基
と、重合可能なビニル基を有する化合物であつ
て、例えば、アクリル酸、メタクリル酸、イタコ
ン酸、無水マレイン酸、2−アクリルアミド−2
−メチルプロパンスルホン酸、スチレンスルホン
酸、ビニルスルホン酸、アリルスルホン酸、メタ
リルスルホン酸等を挙げることが出来る。また、
それらの塩としては、ナトリウム塩、カリウム
塩、アンモニウム塩等が挙げられる。 本発明に係る塩基性ビニル単量体とは、1分子
中に1級アミノ基、2級アミノ基、3級アミノ基
等の塩基性基と、重合可能なビニル基を有する化
合物であつて、例えば、ジメチルアミノエチルメ
タクリレート、ジエチルアミノエチルメタクリレ
ート、ジメチルアミノエチルメタクリレート、ジ
エチルアミノエチルアクリレート、ジメチルアミ
ノプロピルメタクリルアミド、ジメチルアミノプ
ロピルアクリルアミド、2−ビニルピリジン、4
−ビニルピリジン、ジメチルアリルアミン、ジア
リルメチルアミン等を挙げることが出来る。又、
それらの塩、すなわち4級化物としては、水素化
物、メチル化物、エチル化物等であつて、対アニ
オンとして塩素イオン、臭素イオン、水酸基イオ
ン、メチル硫酸基等である化合物が挙げられる。 酸性ビニル単量体と塩基性ビニル単量体の仕込
量比は、モル比で45/55〜55/45である。配合比
が45/55〜55/45の範囲から外れると、生成する
架橋両性共重合体が十分な水との相溶性を持ちえ
ず、分散性能を有さないものとなつてしまう。 本発明に係る架橋性単量体とは、1分子中にビ
ニル基、酸又は塩基と反応しうる官能基を2個以
上有する化合物であつて、例えば、メチレンビス
アクリルアミド、メチレンビスメタクリルアミ
ド、ブタンジオールジアクリレート、ブタンジオ
ールジメタクリレート、エチレングリコールジア
クリレート、エチレングリコールジメタクリレー
ト、ポリエチレングリコールジアクリレート、ポ
リエチレングリコールジメタクリレート、ポリプ
ロピレングリコールジアクリレート、ポリプロピ
レングリコールジメタクリレート、トリメチロー
ルプロパントリアクリレート、トリメチロールプ
ロパントリメタクリレート、アリルアクリルー
ト、アリルメタクリレート、グリシジルアクリレ
ート、グリシジルメタクリレート、2−ヒドロキ
シエチルアクリレート、2−ヒドロキシエチルメ
タクリレート、ジアクリロキシエチルホスフエー
ト、ジメタクリロキシエチルホスフエート、トリ
アリルシアヌレート、トリアリルイソシアヌレー
ト、ジビニルベンゼン、マレイン酸ジアリルエス
テル、ポリアリルサツカロース等を挙げることが
出来る。架橋性単量体の使用量は、全単量体中
0.05〜1モル%である。使用量が少なすぎると、
生成した共重合体は十分満足な分散能が得られ
ず、また多すぎると、生成した共重合体が水に溶
解又は膨潤せず分散剤としては適さない。 共重合反応は従来公知の方法、例えば、塊状重
合、水溶液重合、逆相懸濁重合、沈澱重合などの
方法により遂行することができ、反応温度20〜
120℃、好ましくは35〜80℃でラジカル重合開始
剤の存在下において円滑に行なわれる。 ラジカル重合開始剤としては、過硫酸ナトリウ
ム、過硫酸カリウム、過硫酸アンモニウム、過酸
化ベンゾイル、過酸化水素、過酢酸ナトリウム、
ヒドロ過酸クメン、アゾビスイソブチルニトリル
などが使用される。ラジカル重合開始剤の使用量
はその種類により差はあるが、一般に全単量体に
対し0.01〜5重量%程度が好適である。 本発明の実施にあたつて、酸性ビニル単量体及
び塩基性ビニル単量体以外に、酸性ビニル単量体
及び塩基性ビニル単量体と共重合可能な他のビニ
ル単量体を任意の第3成分として共重合すること
ができるが、全単量体に対し60モル%以下に抑え
ることが必要である。これらビニル単量体はラジ
カル重合開始剤により重合可能なモノビニル化合
物であつて、例えば、アクリル酸メチル、アクリ
ル酸エチル等のアクリル酸エステル類、メタクリ
ル酸メチル、メタクリル酸エチル等のメタクリル
酸エステル類、スチレン、a−メチルスチレン等
のスチレン化合物、アクリルアミド、メタクリル
アミド、ビニルエーテル、酢酸ビニルなどが挙げ
られる。 本発明の架橋両性共重合体からなる分散剤は、
その2重量%溶液(1モル食塩水)の粘度(25
℃)が500〜10000センチポイズの範囲にあり、系
のPH、可溶性塩類の有無にかかわらず、顔料、乳
濁剤、水不溶性殺菌剤、パール化剤、研磨剤など
の水不溶性固体微粒子を安定に分散しうる性能を
有している。特に、上記粘度が1000センチポイズ
以上のものが優れた分散剤である。 かかる優れた効果は従来公知の分散剤として知
られている物には見られない効果であり、いかな
るPH、いかなる可溶性塩の存在下にあつても高い
分散効果を示す高分子物質の製造を本発明が初め
て可能にしたのである。 以下に、実施例により本発明を具体的に説明す
るが、本発明はこれら実施例に限定されるもので
はない。 実施例 1 容量100mlのガラスアンプルを窒素置換し、15
℃以下で、このアンプルに水50g、アクリル酸
7.2g(0.1モル)、ジメチルアミノエチルメタク
リレート15.7g(0.1モル)、メチレンビスアクリ
ルアミド0.03g(0.2ミリモル)及び過硫酸カリ
ウム0.03gを入れ封管する。 封管したアンプルを70℃の恒温槽に浸し、時々
振盪しながら7時間重合を行なう。重合系は全体
がゲル化したものとなるが、これを1のエタノ
ール中に投入し、ホモミキサーで撹拌、粉砕した
後、過、乾燥して白色粉末状の架橋両性共重合
体22g(収率96%)を得た。 得られた架橋両性共重合体を1M食塩水に溶か
し2重量%溶液とし、B型粘度計(1r.p.m.、25
℃)を用いて粘度を測定した。粘度は3200センチ
ポイズであつた。以下の実施例及び比較例中の粘
度はいずれも上記方法による値である。 比較例 1 架橋性単量体であるメチレンビスアクリルアミ
ドを用いない以外は実施例1と同様の操作を行つ
た。白色粉末の両性共重合体(非架橋)22g(96
%)を得た。2重量%溶液(1M食塩水)の粘度
は60センチポイズであつた。 実施例 2 酸性ビニル単量体として2−アクリルアミド−
2−メチルプロパンスルホン酸20.7g(0.1モ
ル)、塩基性ビニル単量体としてジエチルアミノ
エチルメタクリレート18.5g(0.1モル)を用い
る以外は実施例1と同様の操作を行ない、架橋共
重合体37g(収率95%)を得た。 粘度は2300センチポイズであつた。 比較例 2 架橋性単量体のメチレンビスアクリルアミドを
用いない以外は実施例2と同様の操作を行ない、
両性共重合体37g(収率95%)を得た。 粘度は50センチポイズであつた。 実施例 3 酸性ビニル単量体としてスチレンスルホン酸
18.4g(0.1モル)、塩基性ビニル単量体として4
−ビニルピリジン10.5g(0.1モル)及び架橋性
単量体としてエチレングリコールジメタクリレー
ト0.04g(0.2ミリモル)を用い実施例1と同様
の操作を行ない架橋両性共重合体27.7g(収率96
%)を得た。 粘度は1300センチポイズであつた。 比較例 3 架橋性単量体のエチレングリコールジメタクリ
レートを用いない以外は実施例3と同様の操作を
行ない両性共重合体27.7g(収率96%)を得た。
粘度は40センチポイズであつた。 実施例 4 撹拌機、温度計、還流冷却器及び窒素導入管を
付した1−四ツ口フラスコに、ベンゼン500g、
アクリル酸58g(0.8モル)、ジメチルアミノプロ
ピルメタクリルアミド136g(0.8モル)、トリア
リルイソシアヌレート1g(4ミリモル)及びア
ゾビスイソブチロニトリル1gを仕込み、窒素気
流下80℃にて、8時間撹拌を続けた。 最初均一であつた反応系は重合が進むにつれ生
成共重合体の沈澱が生じてくる。反応終了後、沈
澱を過、乾燥し、粉末状の架橋両性共重合体
180g(収率92%)を得た。 粘度は2200センチポイズであつた。 比較例 4 架橋性単量体のトリアリルイソシアヌレートを
用いない以外は実施例4と同様の操作を行ない両
性共重合体178g(収率92%)を得た。 粘度は45センチポイズであつた。 実施例 5 酸性ビニル単量体としてメタリルスルホン酸
109g(0.8モル)、塩基性ビニル単量体としてジ
メチルアミノプロピルメタクリルアミド136g
(0.8モル)及び架橋性単量体としてトリメチロー
ルプロパントリメタクリレート1.35g(4ミリモ
ル)を用いる以外は実施例4と同様の操作を行な
い架橋両性共重合体229g(収率93%)を得た。 粘度は1600センチポイズであつた。 比較例 5 架橋性単量体のトリメチロールプロパントリメ
タクリレートを用いない以外は実施例5と同様の
操作を行ない両性共重合体229g(収率93%)を
得た。 粘度は40センチポイズであつた。 試験例 1 実施例1〜5及び比較例1〜5で合成した架橋
及び非架橋両性共重合体を用い、表1に示す配合
組成(重量%)について分散安定性を調べた。結
果を表1に示す。 (試験法及び評価) 各組成物をガラス製サンプルびんに入れ、50℃
の恒温槽中に1ケ月保存し酢酸ビニル粒子の分散
安定性を肉眼で観察した。 〇:均一に分散 ×:酢酸ビニル粒子が沈澱
The present invention relates to a dispersant comprising a crosslinked amphoteric copolymer. For more details, please refer to cosmetics, cosmetics, pharmaceuticals,
Thickeners and dispersants used in the preparation of emulsions and suspensions, especially cross-linked amphoteric agents that can stably disperse water-insoluble solid particles such as pigments, emulsifiers, water-insoluble bactericides, pearling agents, and abrasives. This invention relates to a dispersant made of a copolymer. Hitherto, various polymer electrolytes have been proposed as thickening/dispersing agents, but none have been necessarily satisfactory. For example, cross-linked polyacrylic acid is a typical example, but when used as a thickening/dispersing agent, if the system is acidic or soluble salts coexist, the viscosity decreases significantly and dispersion performance also decreases. On the other hand, in an attempt to obtain a dispersant that is effective over a wide pH range, Japanese Patent Publication No. 54-3783 proposes an amphoteric copolymer (uncrosslinked). However, the amphoteric copolymers shown therein were not necessarily fully satisfactory in systems where soluble salts were present. Therefore, the present inventors discovered that even in a wide PH range,
As a result of intensive research to obtain a polymer electrolyte that exhibits excellent thickening and dispersing effects even in systems where soluble salts coexist, we found that 45 to 55 mol% of acidic vinyl monomer or its salt and basic vinyl monomer body or its salt 45-55 mol% and crosslinkable monomer 0.05-1 mol%
By copolymerizing a mixed monomer consisting of The present invention was completed by discovering that it is possible to produce a crosslinked amphoteric copolymer that can be dispersed. The acidic vinyl monomer according to the present invention is a compound having an acidic group such as a carboxyl group or a sulfonic acid group and a polymerizable vinyl group in one molecule, such as acrylic acid, methacrylic acid, itaconic acid, etc. , maleic anhydride, 2-acrylamide-2
- Methylpropanesulfonic acid, styrenesulfonic acid, vinylsulfonic acid, allylsulfonic acid, methallylsulfonic acid, etc. can be mentioned. Also,
Examples of these salts include sodium salts, potassium salts, ammonium salts, and the like. The basic vinyl monomer according to the present invention is a compound having a basic group such as a primary amino group, a secondary amino group, a tertiary amino group, and a polymerizable vinyl group in one molecule, and For example, dimethylaminoethyl methacrylate, diethylaminoethyl methacrylate, dimethylaminoethyl methacrylate, diethylaminoethyl acrylate, dimethylaminopropyl methacrylamide, dimethylaminopropylacrylamide, 2-vinylpyridine, 4
-vinylpyridine, dimethylallylamine, diallylmethylamine and the like. or,
Examples of their salts, ie, quaternized products, include hydrides, methylated products, ethylated products, and compounds in which the counter anion is a chlorine ion, bromide ion, hydroxyl ion, methyl sulfate group, etc. The molar ratio of the acidic vinyl monomer to the basic vinyl monomer is 45/55 to 55/45. If the blending ratio is outside the range of 45/55 to 55/45, the resulting crosslinked amphoteric copolymer will not have sufficient compatibility with water and will not have dispersion performance. The crosslinkable monomer according to the present invention is a compound having two or more functional groups capable of reacting with a vinyl group, an acid or a base in one molecule, such as methylenebisacrylamide, methylenebismethacrylamide, butane Diol diacrylate, butanediol dimethacrylate, ethylene glycol diacrylate, ethylene glycol dimethacrylate, polyethylene glycol diacrylate, polyethylene glycol dimethacrylate, polypropylene glycol diacrylate, polypropylene glycol dimethacrylate, trimethylolpropane triacrylate, trimethylolpropane trimethacrylate , allyl acrylate, allyl methacrylate, glycidyl acrylate, glycidyl methacrylate, 2-hydroxyethyl acrylate, 2-hydroxyethyl methacrylate, diacryloxyethyl phosphate, dimethacryloxyethyl phosphate, triallyl cyanurate, triallyl isocyanurate, Examples include divinylbenzene, diallyl maleate, polyallylsucrose, and the like. The amount of crosslinking monomer used is based on the total monomers.
It is 0.05 to 1 mol%. If you use too little,
The produced copolymer does not have a sufficiently satisfactory dispersing ability, and if the amount is too large, the produced copolymer does not dissolve or swell in water, making it unsuitable as a dispersant. The copolymerization reaction can be carried out by conventionally known methods, such as bulk polymerization, aqueous solution polymerization, reversed-phase suspension polymerization, and precipitation polymerization, at a reaction temperature of 20 to
The polymerization is smoothly carried out at 120°C, preferably from 35 to 80°C, in the presence of a radical polymerization initiator. As a radical polymerization initiator, sodium persulfate, potassium persulfate, ammonium persulfate, benzoyl peroxide, hydrogen peroxide, sodium peracetate,
Cumene hydroperacid, azobisisobutylnitrile, etc. are used. The amount of the radical polymerization initiator to be used varies depending on its type, but is generally preferably about 0.01 to 5% by weight based on the total monomers. In carrying out the present invention, in addition to the acidic vinyl monomer and the basic vinyl monomer, any other vinyl monomer copolymerizable with the acidic vinyl monomer and the basic vinyl monomer may be used. Although it can be copolymerized as a third component, it is necessary to suppress it to 60 mol% or less based on the total monomers. These vinyl monomers are monovinyl compounds that can be polymerized with a radical polymerization initiator, and include, for example, acrylic esters such as methyl acrylate and ethyl acrylate; methacrylic esters such as methyl methacrylate and ethyl methacrylate; Examples include styrene, styrene compounds such as a-methylstyrene, acrylamide, methacrylamide, vinyl ether, and vinyl acetate. The dispersant made of the crosslinked amphoteric copolymer of the present invention is
The viscosity of its 2% by weight solution (1 molar saline) (25
°C) is in the range of 500 to 10,000 centipoise, and stabilizes water-insoluble solid particles such as pigments, emulsifiers, water-insoluble bactericides, pearling agents, and abrasives, regardless of system pH and the presence or absence of soluble salts. It has the ability to be dispersed. In particular, those having the above-mentioned viscosity of 1000 centipoise or more are excellent dispersants. Such excellent effects have not been seen in conventionally known dispersants, and we aim to produce polymeric substances that exhibit high dispersion effects at any pH and in the presence of any soluble salts. This invention was made possible for the first time. EXAMPLES The present invention will be specifically explained below with reference to Examples, but the present invention is not limited to these Examples. Example 1 A glass ampoule with a capacity of 100 ml was replaced with nitrogen, and 15
℃ or below, add 50 g of water and acrylic acid to this ampoule.
7.2 g (0.1 mol), dimethylaminoethyl methacrylate 15.7 g (0.1 mol), methylenebisacrylamide 0.03 g (0.2 mmol), and potassium persulfate 0.03 g were placed in the tube and the tube was sealed. The sealed ampoule is immersed in a constant temperature bath at 70°C, and polymerization is carried out for 7 hours with occasional shaking. The entire polymerization system becomes a gel, which is poured into ethanol (1), stirred with a homomixer, pulverized, filtered and dried to obtain 22 g of crosslinked amphoteric copolymer in the form of a white powder (yield: 96%). The obtained crosslinked amphoteric copolymer was dissolved in 1M saline to make a 2% by weight solution, and the solution was measured using a B-type viscometer (1r.pm, 25% by weight).
The viscosity was measured using The viscosity was 3200 centipoise. The viscosities in the following Examples and Comparative Examples are all values determined by the above method. Comparative Example 1 The same operation as in Example 1 was performed except that methylenebisacrylamide, which is a crosslinkable monomer, was not used. White powder amphoteric copolymer (non-crosslinked) 22g (96
%) was obtained. The viscosity of the 2% by weight solution (1M saline) was 60 centipoise. Example 2 2-acrylamide as acidic vinyl monomer
The same operation as in Example 1 was carried out except that 20.7 g (0.1 mol) of 2-methylpropanesulfonic acid and 18.5 g (0.1 mol) of diethylaminoethyl methacrylate were used as the basic vinyl monomer, and 37 g (yield) of the crosslinked copolymer was obtained. 95%). The viscosity was 2300 centipoise. Comparative Example 2 The same operation as Example 2 was carried out except that the crosslinking monomer methylenebisacrylamide was not used.
37 g (yield 95%) of an amphoteric copolymer was obtained. The viscosity was 50 centipoise. Example 3 Styrene sulfonic acid as acidic vinyl monomer
18.4g (0.1mol), 4 as basic vinyl monomer
- The same operation as in Example 1 was carried out using 10.5 g (0.1 mol) of vinylpyridine and 0.04 g (0.2 mmol) of ethylene glycol dimethacrylate as the crosslinkable monomer, resulting in 27.7 g of crosslinked amphoteric copolymer (yield: 96%).
%) was obtained. The viscosity was 1300 centipoise. Comparative Example 3 The same operation as in Example 3 was carried out except that the crosslinkable monomer ethylene glycol dimethacrylate was not used to obtain 27.7 g (yield 96%) of an amphoteric copolymer.
The viscosity was 40 centipoise. Example 4 500 g of benzene,
58 g (0.8 mol) of acrylic acid, 136 g (0.8 mol) of dimethylaminopropyl methacrylamide, 1 g (4 mmol) of triallylisocyanurate, and 1 g of azobisisobutyronitrile were charged, and stirred at 80°C under a nitrogen stream for 8 hours. continued. In the initially homogeneous reaction system, as the polymerization progresses, the resulting copolymer begins to precipitate. After the reaction is complete, the precipitate is filtered and dried to form a powdery crosslinked amphoteric copolymer.
180g (yield 92%) was obtained. The viscosity was 2200 centipoise. Comparative Example 4 178 g (yield: 92%) of an amphoteric copolymer was obtained by carrying out the same operation as in Example 4 except that the crosslinking monomer triallyl isocyanurate was not used. The viscosity was 45 centipoise. Example 5 Methylsulfonic acid as acidic vinyl monomer
109 g (0.8 mol), 136 g dimethylaminopropyl methacrylamide as basic vinyl monomer
(0.8 mol) and 1.35 g (4 mmol) of trimethylolpropane trimethacrylate as the crosslinkable monomer were carried out in the same manner as in Example 4 to obtain 229 g (yield 93%) of a crosslinked amphoteric copolymer. . The viscosity was 1600 centipoise. Comparative Example 5 229 g (yield: 93%) of an amphoteric copolymer was obtained by carrying out the same operation as in Example 5, except that the crosslinkable monomer trimethylolpropane trimethacrylate was not used. The viscosity was 40 centipoise. Test Example 1 Using the crosslinked and non-crosslinked amphoteric copolymers synthesized in Examples 1 to 5 and Comparative Examples 1 to 5, the dispersion stability was investigated for the formulations (wt%) shown in Table 1. The results are shown in Table 1. (Test method and evaluation) Each composition was placed in a glass sample bottle and heated to 50°C.
The dispersion stability of the vinyl acetate particles was observed with the naked eye after storage in a constant temperature bath for one month. 〇: Uniformly dispersed ×: Vinyl acetate particles precipitate

【表】【table】

【表】【table】

【表】 試験例 2 実施例1〜5及び比較例1〜5で合成した架橋
及び非架橋両性共重合体を用い、表2に示す配合
組成(重量%)について分散安定性を調べた。結
果を表2に示す。 (試験法及び評価) 各組成物をガラス製サンプルびんに入れ、50℃
の恒温槽中に1週間保存し、シリカ粉末の分散安
定性を肉眼で観察した。 〇:均一に分散 ×:シリカ粉末が沈澱し、上部はほとんど透明。
[Table] Test Example 2 Using the crosslinked and non-crosslinked amphoteric copolymers synthesized in Examples 1 to 5 and Comparative Examples 1 to 5, the dispersion stability was investigated for the compounding compositions (% by weight) shown in Table 2. The results are shown in Table 2. (Test method and evaluation) Each composition was placed in a glass sample bottle and heated to 50°C.
The dispersion stability of the silica powder was observed with the naked eye. 〇: Uniformly dispersed ×: Silica powder is precipitated, and the upper part is almost transparent.

Claims (1)

【特許請求の範囲】[Claims] 1 酸性ビニル単量体又はその塩45〜55モル%、
塩基性ビニル単量体又はその塩45〜55モル%及び
架橋性単量体0.05〜1モル%からなる混合単量体
を、ラジカル重合開始剤の存在下で20〜120℃の
温度範囲で共重合することにより得られ、2重量
%溶液(1モル食塩水)の粘度(25℃)が500〜
10000センチポイズの範囲にある架橋両性共重合
体からなる分散剤。
1 acidic vinyl monomer or its salt 45-55 mol%,
A monomer mixture consisting of 45 to 55 mol % of a basic vinyl monomer or its salt and 0.05 to 1 mol % of a crosslinkable monomer is co-coated in the temperature range of 20 to 120°C in the presence of a radical polymerization initiator. Obtained by polymerization, the viscosity (25℃) of a 2% by weight solution (1 mol saline) is 500 ~
A dispersant consisting of a crosslinked amphoteric copolymer in the range of 10,000 centipoise.
JP56112576A 1981-07-17 1981-07-17 Preparation of crosslinked ampholytic copolymer Granted JPS5813608A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56112576A JPS5813608A (en) 1981-07-17 1981-07-17 Preparation of crosslinked ampholytic copolymer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56112576A JPS5813608A (en) 1981-07-17 1981-07-17 Preparation of crosslinked ampholytic copolymer

Publications (2)

Publication Number Publication Date
JPS5813608A JPS5813608A (en) 1983-01-26
JPH0324254B2 true JPH0324254B2 (en) 1991-04-02

Family

ID=14590172

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56112576A Granted JPS5813608A (en) 1981-07-17 1981-07-17 Preparation of crosslinked ampholytic copolymer

Country Status (1)

Country Link
JP (1) JPS5813608A (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58127714A (en) * 1982-01-25 1983-07-29 Kyoritsu Yuki Kogyo Kenkyusho:Kk Production of highly water-absorbing polymer
JPS58154710A (en) * 1982-03-09 1983-09-14 Kyoritsu Yuki Kogyo Kenkyusho:Kk Production of amphoteric, highly water-absorptive resin
FR2595706B1 (en) * 1986-03-14 1988-05-27 Protex Manuf Prod Chimiq NOVEL CROSSLINKED CARBOXYLIC COPOLYMERS FOR USE AS THICKENERS IN AQUEOUS MEDIA AND THEIR PREPARATION
GB8721698D0 (en) * 1987-09-15 1987-10-21 Shell Int Research Polymeric surfactants
US4910249A (en) * 1988-05-02 1990-03-20 Ppg Industries, Inc. Acrylic polymers
JPH0713191B2 (en) * 1989-11-27 1995-02-15 東洋紡績株式会社 Resin particles and method for producing the same
DE10052176B4 (en) 1999-10-21 2004-07-08 Kabushiki Kaisha Toshiba, Kawasaki Steam turbine rotor and method of manufacturing the same

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4933737A (en) * 1972-07-28 1974-03-28
CS177507B1 (en) * 1974-02-12 1977-07-29
JPS52127995A (en) * 1976-04-19 1977-10-27 Johnson & Johnson Hydrophilic random copolymers composition and process for producing same
JPS548788A (en) * 1977-06-15 1979-01-23 Nitto Boseki Co Ltd Immobilization of enzymes or microbial cells with ampholytic polymer

Also Published As

Publication number Publication date
JPS5813608A (en) 1983-01-26

Similar Documents

Publication Publication Date Title
US7208556B2 (en) Water-soluble or water-swellable crosslinked copolymers
CA2123460C (en) Method for the production of a low-viscosity, water-soluble polymeric dispersion
EP0101920B1 (en) Liquid detergent composition
US4722958A (en) Process for the preparation of copolymers
US5844039A (en) Polymers comprising reversible hydrophobic functionalities
EP0346834B1 (en) Process for the manufacture of polymers
JPH07258305A (en) Production of lowly viscous water-soluble polymer dispersion, and flocculant, retentive, thickener, additive, dehydrator and soil conditioner comprising same
JPS62232413A (en) Production and use of fine powdery crosslinked copolymer
JPS6181415A (en) Cationic high polymer electrolyte and manufacture
JPH0324254B2 (en)
JPH09157130A (en) Water soluble thickener and cosmetic material blended with the same
GB2084585A (en) The Preparation of High Molecular Weight Hydrophilic Polymer Gels
KR100447838B1 (en) Carboxylated polymer composition
JP4286448B2 (en) Polymerization process and product and product use
US6794467B2 (en) Process for the preparation of polymeric absorbents
Kaçmaz et al. Swelling Behavior of N‐t‐butylacrylamide Copolymer and Terpolymers
JPS5813609A (en) Preparation of crosslinked ampholytic polymer
JPH01168703A (en) Dispersant for reverse phase suspension polymerization
JPH04130113A (en) Production of macrobead-like water-absorptive resin
JPH062769B2 (en) Method for producing super absorbent polymer with excellent salt resistance
JP2003246909A (en) Polymer dispersion and method for producing the same
JP2002121223A (en) Polymer and method for producing the same
JPH01236211A (en) Production of quaternary salt of vinylpyrrolidone copolymer
JPH0393815A (en) Water-absorbing resin composition
CA2033787C (en) Crosslinked carboxylic copolymers useful as thickeners