JPS5853940A - Preparation of hydrosol - Google Patents

Preparation of hydrosol

Info

Publication number
JPS5853940A
JPS5853940A JP15332181A JP15332181A JPS5853940A JP S5853940 A JPS5853940 A JP S5853940A JP 15332181 A JP15332181 A JP 15332181A JP 15332181 A JP15332181 A JP 15332181A JP S5853940 A JPS5853940 A JP S5853940A
Authority
JP
Japan
Prior art keywords
copolymer
solvent
water
weight
hydrosil
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
JP15332181A
Other languages
Japanese (ja)
Other versions
JPS6031329B2 (en
Inventor
Shinji Yoshikawa
吉川 信治
Isao So
宗 伊佐雄
Takao Yoshikawa
吉川 孝雄
Makoto Sunakawa
砂川 誠
Michio Satsuma
道夫 薩摩
Ichiro Ijichi
伊地知 市郎
Shinji Yamada
進治 山田
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.)
Nitto Denko Corp
Original Assignee
Nitto Electric Industrial 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 Nitto Electric Industrial Co Ltd filed Critical Nitto Electric Industrial Co Ltd
Priority to JP56153321A priority Critical patent/JPS6031329B2/en
Publication of JPS5853940A publication Critical patent/JPS5853940A/en
Publication of JPS6031329B2 publication Critical patent/JPS6031329B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Processes Of Treating Macromolecular Substances (AREA)
  • Colloid Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Paints Or Removers (AREA)
  • Paper (AREA)

Abstract

PURPOSE:To prepare a hydrosol capable of forming a coating film or formed article having excellent water resistance and high physical properties, by neutralizing a specific high-molecular copolymer synthesized in the absence of solvent or in the presence of a small amount of solvent, and dispersing the neutralized product in water by phase inversion. CONSTITUTION:A copolymer having a weight-average molecular weight of 10<4>- 10<6> and composed of 1-20wt% unsaturated monomer having acidic group and 99-80% other unsaturated monomer copolymerizable therewith, is synthesized in the absence of solvent or in the presence of a small amount of solvent. An alkali or an alkaline aqueous solution is added to the copolymer to neutralize a part of or the whole acidic groups in said copolymer, and the product is subjected to the phase inversion by adding water. A hydrosol of the copolymer having an average particle diameter of 0.01-0.1mum and dispersed stably in water can be obtained by this process. The solvent is preferably methanol, etc., and its amount is <=20%. The monomer having acidic group is e.g. acrylic acid, etc., and the copolymerizable monomer is an acrylic acid ester having 3-10C alkyl group.

Description

【発明の詳細な説明】 この発明はヒドロシルつまり粒子径0.01〜0.1μ
mの重合体粒子が水中に安定に分散された分散体の新し
い製造方法、とくに無溶剤ないし少量の溶剤の存在下で
合成された比較的高分子量の重合体をヒドロシル化する
ことを特徴とする新規な製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION This invention provides hydrosil particles with a particle size of 0.01 to 0.1μ.
A new method for producing a dispersion in which polymer particles of m are stably dispersed in water, and is characterized by hydrosilating a relatively high molecular weight polymer synthesized without a solvent or in the presence of a small amount of solvent. Concerning a new manufacturing method.

従来、ヒドロシルの製造方法としては、たとえば特公昭
46−22343号公報、特開昭50−19842号公
報などにみられる如く、エマルション重合法により得た
カルボキシル基を有する重合体粒子(粒径約0.3〜0
7μm)を苛性カリ、苛性ソーダ、水酸化アンモニウム
などのアルカリを用いて高速攪拌上粒子表面を削り取り
、粒径約0.01〜0.1μmの微細粒子にするという
、いわゆるストリッパブルの手法が一般的に採用されて
きた。
Conventionally, methods for producing hydrosil include polymer particles having a carboxyl group (particle size of approximately 0.0 .3~0
The so-called strippable method is generally used, in which the surface of particles (7 μm) is scraped off while stirring at high speed using an alkali such as caustic potash, caustic soda, or ammonium hydroxide to make fine particles with a particle size of approximately 0.01 to 0.1 μm. It has been adopted.

ところが、」1記従来法によると、ヒドロシル中に乳化
剤が混入してくるため、これより得られる塗膜その他の
成形物のil+il水性が悪くなる。また、ヒドロシル
化しうる重合体の分子量に制限があり、一般に重量平均
分子量が104(1万)以−■−になるとヒドロシル化
が難しくなる。このため、各種用途への応用面で自ずと
限界を生じ、主に塗料分野や紙サイズ処理分野への応用
展開しか計れなかった。
However, according to the conventional method described in item 1, emulsifiers are mixed into the hydrosil, which deteriorates the il+il aqueous properties of coating films and other molded products obtained therefrom. Further, there is a limit to the molecular weight of a polymer that can be hydrosilated, and generally, when the weight average molecular weight is 104 (10,000) or more, hydrosilation becomes difficult. For this reason, there was a natural limit in terms of application to various uses, and applications could only be developed mainly in the paint field and paper size processing field.

この発明は、上記従来の欠点を回避することを目的とし
てなされたものであり、その要旨とするところは、無溶
剤ないし少量の溶剤の存在下で、酸性基を有する不飽和
単量体1〜20重量%とこれと共重合可能な他の不飽和
単量体99〜80重量%とからなる重量平均分子量10
4〜106の共重合体を合成し、これにアルカリないし
アルカリ水溶液を加えて上記共重合体分子中の酸性基の
1部または全部を中和し、そのごさらに水を加えて転相
させ上記共重合体が平均粒子径001〜0.1μmの範
囲で水中に安定に分散されたヒドロシルを得ることを特
徴とするヒドロシルの製造方法にある。
This invention was made with the aim of avoiding the above-mentioned conventional drawbacks, and its gist is that unsaturated monomers 1- Weight average molecular weight 10 consisting of 20% by weight and 99 to 80% by weight of other unsaturated monomers copolymerizable therewith.
Synthesize a copolymer of 4 to 106, add an alkali or aqueous alkali solution to neutralize part or all of the acidic groups in the copolymer molecule, and further add water to phase invert the above. A method for producing hydrosil, characterized by obtaining hydrosil in which a copolymer is stably dispersed in water with an average particle diameter in the range of 001 to 0.1 μm.

すなわち、この発明者らは、従来のように重合体エマル
ジョンを使用するのではなく、塊状重合ないし少量の溶
剤を用いた溶液重合により得られる酸性基を有する特定
の共重合体でその分子量か比較的高いものを使用し、こ
れをアルカリないしアルカリ水溶液で適当に中和したの
ち、さらに水を加えて転相させることにより、上記共重
合体が平均粒子径0.01〜0.1μmの範囲で水中に
安定に分散されたヒドロシルを得ることに成功したもの
である。
That is, the inventors compared the molecular weight of a specific copolymer with acidic groups obtained by bulk polymerization or solution polymerization using a small amount of solvent, rather than using a polymer emulsion as in the past. After neutralizing the copolymer with an alkali or alkaline aqueous solution, the above copolymer has an average particle size in the range of 0.01 to 0.1 μm by adding water and inverting the phase. We succeeded in obtaining hydrosil stably dispersed in water.

このようにして得られるこの発明に係るヒドロシルは、
これを塗膜その他の成形物としたときに、従来のヒドロ
シルに較べてはるかに改善された111iJ水性を示し
、また重合体の分子量が比較的高いものであることから
各種物理特性も良好で、一般の有機溶剤溶液から形成さ
れる塗膜なとと変らないすぐれた性能を発揮Jる。この
ため、従来のヒドロシルよりも応用範囲が広くなり、塗
料や紙→ノーイズ処理剤はもちろん、粘着剤、接着剤、
オーバーコート剤、外装材、内装拐、包装材、フィルム
などの各種分野に極めて有効に適用することかできる。
The hydrosil according to the present invention obtained in this way is
When made into coatings or other molded products, it exhibits a much improved 111iJ aqueous property compared to conventional hydrosils, and since the molecular weight of the polymer is relatively high, it also has good physical properties. It exhibits the same excellent performance as coating films formed from general organic solvent solutions. For this reason, the range of applications is wider than that of conventional hydrosils, from paint and paper to noise treatment agents, as well as adhesives, adhesives, etc.
It can be extremely effectively applied to various fields such as overcoating agents, exterior materials, interior coatings, packaging materials, and films.

この発明においては、まず、無溶剤ないし少量の溶剤の
存在下で、酸性基を有する不飽和単量体1〜20重量%
とこれと共重合可能な他の不飽和単量体99〜80重量
%とからなる重量平均分子M104〜106の共重合体
を合成する。
In this invention, first, 1 to 20% by weight of an unsaturated monomer having an acidic group is added in the absence of a solvent or in the presence of a small amount of a solvent.
and 99 to 80% by weight of other unsaturated monomers copolymerizable with this, and a weight average molecular weight M104 to M106 copolymer is synthesized.

溶剤の使用は、塊状重合しにくい単量体組成の場合ある
いは粘度調節を容易にするためなどの目的で用いられる
が、その使用量は通常20重量%以下とされているのが
よい。また、ここで用いられる溶剤としては、一般の有
機溶剤を種々使用できるが、好ましくはメタノール、エ
タノール、n−フタノール、n−プロパツール、イソプ
ロピルアルコール、5eC−フタノールナトのアルコー
ル系親水性溶媒か、あるいは水酸基、カルボキシル基、
アミ7基などの親水基を有するオリゴマーないしプレポ
リマーの使用が望ましい。
A solvent is used in the case of a monomer composition that is difficult to undergo bulk polymerization or for the purpose of facilitating viscosity control, but the amount used is usually 20% by weight or less. As the solvent used here, various general organic solvents can be used, but preferably alcoholic hydrophilic solvents such as methanol, ethanol, n-phthanol, n-propanol, isopropyl alcohol, and 5eC-phthanol, or hydroxyl group, carboxyl group,
It is desirable to use an oligomer or prepolymer having a hydrophilic group such as amide 7 group.

単量体成分中とくに重要な酸性基を有する不飽和単量体
としては、たとえばアクリル酸、メタクリル酸、クロト
ン酸、イタコン酸、マレイン酸、フマル酸などの酸性基
としてカルボキシル基を有する不飽和カルボン酸、スチ
レンスルホン酸、アリルスルホン酸、スルホプロピルア
クリレート、2−アクリロイルオキシナフタレン−2−
スルホン酸、2−メタクリロイルオキシナフタレン−2
−スルホン酸、2−アクリルアミド−2−メチルプロパ
ンスルホン酸、2−アクリロイルオキシベンゼンスルホ
ン酸などの酸性基としてスルホン基を有する不飽和スル
ホン酸などを挙げることができ、またその他の酸性基を
有するものであってもよく、これらの1種もしくは2種
以」―を使用する。
Examples of unsaturated monomers having particularly important acidic groups in the monomer components include unsaturated carboxylic acid having a carboxyl group as an acidic group, such as acrylic acid, methacrylic acid, crotonic acid, itaconic acid, maleic acid, and fumaric acid. acid, styrene sulfonic acid, allyl sulfonic acid, sulfopropyl acrylate, 2-acryloyloxynaphthalene-2-
Sulfonic acid, 2-methacryloyloxynaphthalene-2
Examples of acidic groups include unsaturated sulfonic acids having a sulfonic group, such as -sulfonic acid, 2-acrylamido-2-methylpropanesulfonic acid, and 2-acryloyloxybenzenesulfonic acid, and other acids having an acidic group. One or more of these may be used.

」−記不飽和単量体の使用量は、全単量体中1〜20屯
量%とする必要があり、たとえば不飽和カルボン酸の場
合とくに好適にc」5〜15重量J、また、不飽和スル
ホン酸の場合とくcこ好適には3〜10重量%である。
The amount of unsaturated monomers to be used should be 1 to 20 tonne % based on the total monomers, for example, in the case of unsaturated carboxylic acids, it is particularly preferable to use 5 to 15 wt. Especially in the case of unsaturated sulfonic acids, it is preferably from 3 to 10% by weight.

この使用量が1重量%に満たないかあるいは20重量%
を越えてしまうと、いずれもヒドロシル化に好結果が7
4+ ’yれない。
This usage amount is less than 1% by weight or 20% by weight
If it exceeds 7, good results are obtained for hydrosylation.
4+ 'I can't do it.

このような不飽和単量体と併用される共重合可能な他の
不飽和単量体としては、各種のエチレン性不飽和単量体
のなかから任意に選択できる。たとえばアルキル基の炭
素数1〜15、とくに好適には3〜10のアクリル酸エ
ステルやメタクリル酸エステル、その他ビニルエーテル
、ビニルエステノペアクリロニトリル、アクリルアミド
、ヒドロキシアルキルアクリレート、スチレン、塩化ビ
ニル、エチレン、分子内にアミン基の如き官能基を有す
るエチレン性不飽和単量体などを挙げることができ、用
途目的に応じてその1種または2種リ、上を選択して使
用する。
Other copolymerizable unsaturated monomers used in combination with such unsaturated monomers can be arbitrarily selected from various ethylenically unsaturated monomers. For example, an alkyl group having 1 to 15 carbon atoms, preferably 3 to 10 carbon atoms, acrylic esters and methacrylic esters, other vinyl ethers, vinyl esterophores, acrylonitrile, acrylamide, hydroxyalkyl acrylates, styrene, vinyl chloride, ethylene, intramolecular Examples include ethylenically unsaturated monomers having a functional group such as an amine group, and one or two of them are selected and used depending on the purpose of use.

無溶剤ちいし少量の溶剤を用いた共重合体の合成は、従
来公知の方法により、」1記の各単量体を反応器に仕込
んで窒素置換し、有機過酸化物やアゾ化合物の如き適宜
の重合開始剤を使用し、また必要ならメルカプタンの如
き重合調節剤を用いて加熱重合させればよい。このとき
、所望により、反応器中に予め粘着付与剤、軟化剤、可
争剤、充填剤、顔料類などの添加剤を添加しておいても
よい。これらの添加剤は、共重合体の合成ごに添加する
こともできる。
Synthesis of a copolymer using a small amount of solvent is carried out by a conventionally known method. Each of the monomers described in 1. is charged into a reactor, the atmosphere is replaced with nitrogen, and organic peroxides, azo compounds, etc. The polymerization may be carried out by heating using an appropriate polymerization initiator and, if necessary, a polymerization regulator such as mercaptan. At this time, if desired, additives such as tackifiers, softeners, movable agents, fillers, and pigments may be added in advance to the reactor. These additives can also be added each time the copolymer is synthesized.

上記方法で合成される共重合体はその重量平均分子量か
104〜106の範囲に設定されていることが必要であ
る。この理由はつぎのとおりであり、104に満たない
場合は、塗膜その他の成形物としたときの物性、たとえ
は凝集力や物理的強度などに劣り、また106を越える
ようでは高粘度となってそのこのアルカリ処理に支障を
きたし、ヒドロシルを生成しに(くなるからである。
It is necessary that the weight average molecular weight of the copolymer synthesized by the above method is set within the range of 104 to 106. The reason for this is as follows: if it is less than 104, the physical properties, such as cohesive force and physical strength, will be poor when made into a coating or other molded product, and if it exceeds 106, it will have a high viscosity. This is because it interferes with this alkali treatment and tends to generate hydrosil.

この発明においては、つぎに、上述の如き分子量を有し
かつ前記少量の溶剤を含むことがある共重合体中に、攪
拌下、アルカリまたはアルカリ水溶液を加えて中和処理
する。このときの処理温度は共重合体の種類、性状に応
じて一定温度下に保たれるが、一般には40〜95゛C
である。中和処理に用いるアルカリないしアルカリ水溶
液としては、アンモニア、アンモニア水、苛性ソータ、
苛性カリなどの苛性アルカリの水溶液などがあり、通常
共重合体のカルボキシル基やスルホン基の如き酸性基に
対して約1150〜2当量の割合で使用すればよい。
In the present invention, an alkali or aqueous alkali solution is then added to the copolymer having the molecular weight as described above and which may contain a small amount of the solvent to neutralize the copolymer while stirring. The treatment temperature at this time is kept at a constant temperature depending on the type and properties of the copolymer, but it is generally 40-95°C.
It is. Alkali or aqueous alkaline solutions used for neutralization include ammonia, aqueous ammonia, caustic sorter,
Examples include aqueous solutions of caustic alkalis such as caustic potash, and they may be used in an amount of about 1150 to 2 equivalents relative to acidic groups such as carboxyl groups and sulfone groups in the copolymer.

このように中和処理したのち、さらに攪拌を続けてよく
混合しなから、水を徐々に加えていくと、一定時間こ゛
にいわゆる転相現象がおこり、水が連続層となりこのな
かに共重合体粒子か分散された0/W型の分散体が生成
する。この分散停生成ご、さらに必要量の水を徐々に冷
加し、分イ1+体の粘度と固形分濃度を調節する。この
粘jす:は一般に25゛Cで30〜1,000ポイズで
あり、また固形分濃度は通常10〜60市量%である。
After this neutralization treatment, if you continue stirring to mix well and then gradually add water, a so-called phase inversion phenomenon will occur for a certain period of time, and water will form a continuous layer and copolymerize in this layer. An 0/W type dispersion in which the combined particles are dispersed is produced. After this dispersion is stopped, a necessary amount of water is gradually cooled to adjust the viscosity and solid content concentration of the dispersion. The viscosity is generally 30 to 1,000 poise at 25°C, and the solids concentration is usually 10 to 60% by market weight.

かくして得られる分散体は、分散粒子である共重合体の
平均粒子径が0.01〜0.1μmとされ、この共重合
体粒子が水中に均一にかつ安定に分散されたヒドロシル
であり、これを単独であるいは架橋剤などを加えて担体
上に流延し乾燥して塗膜化したときに、またその他の成
形物に硬化成形したときに、前述のとおりのすぐれた性
能を発揮する。
The dispersion thus obtained is a hydrosil in which the average particle diameter of the copolymer as the dispersed particles is 0.01 to 0.1 μm, and the copolymer particles are uniformly and stably dispersed in water. It exhibits the above-mentioned excellent performance when it is cast alone or with the addition of a crosslinking agent etc. onto a carrier and dried to form a coating film, or when it is cured and molded into other molded products.

以下に、この発明の実施例を記載する。Examples of this invention will be described below.

実施例1 メタクリル酸n−ブチル    60gアクリル酸エチ
ル       60Qメタクリル酸        
 15gアゾビス吉草酸        015gラウ
リルメルカプタン     0.075 g上記の組成
物のうちの15&を11の四つ目フラスコに仕込み、攪
拌しなから40分間窒素置換した。そのこ滴下ロートか
ら残量を滴下しなから83°Cで4時間反応させ、重量
平均分子量8×105(GPCによる)の共重合体を合
成した。
Example 1 n-butyl methacrylate 60g ethyl acrylate 60Q methacrylic acid
15g azobisvaleric acid 015g lauryl mercaptan 0.075g 15& of the above compositions were charged into a fourth flask (No. 11), and the flask was purged with nitrogen for 40 minutes without stirring. The remaining amount was added dropwise from the dropping funnel and the mixture was reacted at 83°C for 4 hours to synthesize a copolymer with a weight average molecular weight of 8 x 105 (according to GPC).

つぎに、この共重合体のカルボキシル基に対して1/1
6当量の苛性ソーダ水溶液(20重量%)を加えて86
°Cの温度下で中和処理し、そのこ、さらに攪拌しなが
ら、共重合体100部に対して250部の水を約2時間
髪して徐々に滴下した。
Next, 1/1 to the carboxyl group of this copolymer
86 by adding 6 equivalents of caustic soda aqueous solution (20% by weight)
The mixture was neutralized at a temperature of .degree. C., and 250 parts of water was gradually added dropwise to 100 parts of the copolymer for about 2 hours while stirring.

150部の水を滴下した時点で、連続層が水となる転相
現象が生じた。
When 150 parts of water was added dropwise, a phase inversion phenomenon occurred in which the continuous layer became water.

このようにして得られたヒドロシルは、その粘度(25
”C)が175ポイズ、固形分濃度が26.5重量%で
、平均粒子径が0.08μm(ナノサイザー加熱乾燥を
行なって、50μm厚の皮膜を形成した。
The hydrosil thus obtained has a viscosity (25
"C) had a solid content of 175 poise, a solid content concentration of 26.5% by weight, and an average particle diameter of 0.08 μm (heat drying with a nanosizer was performed to form a film with a thickness of 50 μm.

この皮膜の耐水性およびその他の特性を調べた結果はつ
ぎの第1表に示されるとおりであった。
The results of examining the water resistance and other properties of this film are shown in Table 1 below.

(注)1)実施例1と同組成の単量体混合物を、連鎖移
動剤としてチオグリコール酸を、重合開始剤として過硫
酸カリウムを用いて乳化重合して得た重量平均分子量2
×104の重合体エマルジョンから作成した皮膜の試験
結果である。
(Note) 1) Weight average molecular weight 2 obtained by emulsion polymerization of a monomer mixture having the same composition as in Example 1 using thioglycolic acid as a chain transfer agent and potassium persulfate as a polymerization initiator.
This is a test result of a film made from a polymer emulsion of x104.

2)引張速度5 Q mm 7分における測定値である
2) Measured values at a tensile speed of 5 Q mm and 7 minutes.

実施例2 アクリル酸n−オクチル    651i’メタクリル
酸メチル      35gアクリル酸       
    10gアゾビスイソブチロニトリル   0.
1g5ec−ブタノール        5g上記組成
のうち、モノマー混合物の10ダと5ec−7’タノ一
ル5gとを11の四つ目フラスコに仕込み、攪拌しなか
ら40゛Cで40分間窒素置換した。そのご、アゾビス
イソブチロニトリル0.1gを添加し、完全に溶解して
から80°Cに昇温した。ついで、残りのモノマー混合
物を滴下ロー1・から約0.871i’/分の速度で2
時間髪して滴下し、85部5℃で4時間反応させ、重量
平均分子量6.5 X l 05 (GI’Cによる)
の共重合体を合成した。
Example 2 n-octyl acrylate 651i' methyl methacrylate 35g acrylic acid
10g azobisisobutyronitrile 0.
1 g 5 ec-butanol 5 g Of the above composition, 10 Da of the monomer mixture and 5 g of 5 ec-7' tanol were charged into a fourth flask (No. 11), and the flask was purged with nitrogen at 40° C. for 40 minutes without stirring. Then, 0.1 g of azobisisobutyronitrile was added, and after completely dissolving, the temperature was raised to 80°C. The remaining monomer mixture is then added to the dropping roller from 1 to 2 at a rate of about 0.871 i'/min.
85 parts were added dropwise to the hair for 4 hours and reacted at 5°C for 4 hours to obtain a weight average molecular weight of 6.5 x 105 (according to GI'C).
A copolymer was synthesized.

つきに、この共重合体のカルボキシル基に対して1/8
当量のアンモニア水溶液(25重量%)を加えて80部
3°Cの温度下で中和処理し、そのご、さらに攪拌しな
から、共重合体100部に対して200部の水を約2時
間髪して徐々に滴下した。120部の水を滴下した時点
で、連続層が水となる転相現象が生じた。
At the same time, 1/8 of the carboxyl group of this copolymer
Add an equivalent amount of ammonia aqueous solution (25% by weight) to neutralize 80 parts at a temperature of 3°C, and then, without further stirring, add about 200 parts of water to 100 parts of the copolymer. I applied it to my hair for an hour and then gradually dripped it. When 120 parts of water was added dropwise, a phase inversion phenomenon occurred in which the continuous layer became water.

このようにして得られたヒドロシルは、その粘度(25
”C)が270ボイス、固形分濃度が34.9重量%で
、平均粒子径が0.06μn)であった。このヒドロシ
ルを用いて、以下実施例1にしたかつて皮膜を作成し、
実施例1と同様に特性評価を行なった結果は、後記の第
2表に示されるとおりであった。
The hydrosil thus obtained has a viscosity (25
"C) had 270 voices, a solid content concentration of 34.9% by weight, and an average particle size of 0.06 μn). Using this hydrosil, a film was prepared as shown in Example 1 below,
The characteristics were evaluated in the same manner as in Example 1, and the results were as shown in Table 2 below.

実施例3 アクリル酸n−オクチル    65gメタクリル酸メ
チル      35gアクリル酸         
  2gアゾビスイソブチロニトリル   0.1if
sec−ブタノール        5g上記の原料組
成で、実施例2と同様の操作にて共重合反応を行ない、
重量平均分子量6×105(GPCによる)の共重合体
を合成した。
Example 3 n-octyl acrylate 65g methyl methacrylate 35g acrylic acid
2g azobisisobutyronitrile 0.1if
sec-butanol 5g With the above raw material composition, a copolymerization reaction was carried out in the same manner as in Example 2,
A copolymer with a weight average molecular weight of 6 x 105 (according to GPC) was synthesized.

この共重合体をこれに含まれるカルボキシル基に対して
1当量のアンモニア水溶液(25重量%)を用いて実施
例2と同様にして中和処理し、そのと、さらに攪拌しな
がら、共重合体100部に対して300部の水を徐々に
滴下した。180部の水を滴下した時点で、連続相が水
となる転相現象が生じた。
This copolymer was neutralized in the same manner as in Example 2 using an ammonia aqueous solution (25% by weight) of 1 equivalent to the carboxyl group contained therein, and then, while stirring, the copolymer was 300 parts of water was gradually added dropwise to 100 parts. When 180 parts of water was added dropwise, a phase inversion phenomenon occurred in which the continuous phase became water.

このようにして得られたヒドロシルは、その粘度(25
”C)が55ボイズ、固形分濃度か25.1重量%で、
平均粒子径が0.09μmであった。このヒドロシルを
用いて、以下実施例1にしたがって皮膜を形成し、実施
例1と同様に特性評価を行なった結果は、後記の第2表
に示されるとおりであった。
The hydrosil thus obtained has a viscosity (25
``C) has 55 voids, solid content concentration is 25.1% by weight,
The average particle diameter was 0.09 μm. Using this hydrosil, a film was formed according to Example 1, and the characteristics were evaluated in the same manner as in Example 1. The results were as shown in Table 2 below.

実施例4 アクリル酸n−オクチル    65gメタクリル酸メ
チル      35gアクリル酸         
  20gアゾビスイソブチロニトリル   0.19
sec−ブタノール        5g上記の原料組
成で、実施例2と同様の操作にて共重合反応を行ない、
重量平均分子量6.8X105(G l’ Cによる)
の共重合体を合成した。
Example 4 n-octyl acrylate 65g methyl methacrylate 35g acrylic acid
20g Azobisisobutyronitrile 0.19
sec-butanol 5g With the above raw material composition, a copolymerization reaction was carried out in the same manner as in Example 2,
Weight average molecular weight 6.8X105 (according to G l' C)
A copolymer was synthesized.

この共重合体をこれに含まれるカルボキシル基に対して
1/20当量のアンモニア水溶液(25重量%)を用い
て実施例2と同様にして中和処理し、そのこ、さらに攪
拌しなから共重合体100部に対して150部の水を徐
々に滴下した。80部の水を滴下した時点で、連続相か
水となる転相現象か生じた。
This copolymer was neutralized in the same manner as in Example 2 using an ammonia aqueous solution (25% by weight) in an amount of 1/20 equivalent to the carboxyl groups contained in the copolymer. 150 parts of water was gradually added dropwise to 100 parts of the polymer. When 80 parts of water was added dropwise, a phase inversion phenomenon occurred in which the continuous phase changed to water.

このようにして得られたヒドロシルは、その粘度(25
”C)が370ボイズ、固形分濃度が43.6重量%で
、平均粒子径が0.03μmであった。このヒドロシル
を用いて、以下実施例1にしたがって皮膜を形成し、実
施例1と同様に特性評価を行なった結果6]、つきの第
2表に示されるとおりであった。
The hydrosil thus obtained has a viscosity (25
"C) had 370 voids, a solid content concentration of 43.6% by weight, and an average particle diameter of 0.03 μm. Using this hydrosil, a film was formed according to Example 1, and The results of the characteristic evaluation conducted in the same manner [6] were as shown in Table 2.

第2表 以上の試験結果から明らかなように、この発明法により
得たヒドロシルによれは、耐水性にすぐれる皮膜を形成
でき、また支棒の機械的特性も充分に満足できるもので
あることが判る。
As is clear from the test results in Table 2 and above, the hydrosil obtained by the method of this invention can form a film with excellent water resistance, and the mechanical properties of the support rod are also fully satisfactory. I understand.

特許出願人  日東電気工業株式会社Patent applicant: Nitto Electric Industry Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] (1)無溶剤ないし少量の溶剤の存在下で、酸性基を有
する不飽和単量体1〜20重量%とごれと共重合可能な
他の不飽和単量体99〜80重量%とからなる重量平均
分子量104〜106の共重合体を合成し、これにアル
カリないしアルカリ水溶液を加えて上記共重合体分子中
の酸性基の1部または全部を中和し、そのこさらに水を
加えて転相させ上記共重合体が平均粒子径0.01〜0
.1μmの範囲で水中に安定に分散されたヒドロシルを
得ることを特徴とするヒドロシルの製造方法。
(1) In the presence of no solvent or a small amount of solvent, from 1 to 20% by weight of an unsaturated monomer having an acidic group and 99 to 80% by weight of another unsaturated monomer that can copolymerize with dirt. Synthesize a copolymer having a weight average molecular weight of 104 to 106, add an alkali or aqueous alkali solution to neutralize part or all of the acidic groups in the copolymer molecule, and further add water. By phase inversion, the above copolymer has an average particle size of 0.01 to 0.
.. A method for producing hydrosil, characterized by obtaining hydrosil stably dispersed in water in a range of 1 μm.
JP56153321A 1981-09-28 1981-09-28 Hydrosol production method Expired JPS6031329B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56153321A JPS6031329B2 (en) 1981-09-28 1981-09-28 Hydrosol production method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56153321A JPS6031329B2 (en) 1981-09-28 1981-09-28 Hydrosol production method

Publications (2)

Publication Number Publication Date
JPS5853940A true JPS5853940A (en) 1983-03-30
JPS6031329B2 JPS6031329B2 (en) 1985-07-22

Family

ID=15559933

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56153321A Expired JPS6031329B2 (en) 1981-09-28 1981-09-28 Hydrosol production method

Country Status (1)

Country Link
JP (1) JPS6031329B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61261369A (en) * 1985-05-16 1986-11-19 Asahi Chem Ind Co Ltd Paint for artificial turf
JPS63183968A (en) * 1987-01-27 1988-07-29 Toyo Seikan Kaisha Ltd Production of emulsion type water based paint
JPS63183969A (en) * 1987-01-27 1988-07-29 Toyo Seikan Kaisha Ltd Production of emulsion type water based paint
US5166254A (en) * 1990-12-03 1992-11-24 E. I. Du Pont De Nemours And Company Waterbased coating composition of methylol (meth)acrylamide acrylic polymer, acrylic hydrosol and melamine crosslinking agent
JP2004307850A (en) * 2003-03-25 2004-11-04 Nippon Paint Co Ltd Production process of internally cross-linked fine particle resin containing o/w type emulsion, cation electrodeposition coating composition and coated product

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55142044A (en) * 1979-04-24 1980-11-06 Nippon Shokubai Kagaku Kogyo Co Ltd Aqueous dispersion for floor polishing composition

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55142044A (en) * 1979-04-24 1980-11-06 Nippon Shokubai Kagaku Kogyo Co Ltd Aqueous dispersion for floor polishing composition

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61261369A (en) * 1985-05-16 1986-11-19 Asahi Chem Ind Co Ltd Paint for artificial turf
JPS63183968A (en) * 1987-01-27 1988-07-29 Toyo Seikan Kaisha Ltd Production of emulsion type water based paint
JPS63183969A (en) * 1987-01-27 1988-07-29 Toyo Seikan Kaisha Ltd Production of emulsion type water based paint
US5166254A (en) * 1990-12-03 1992-11-24 E. I. Du Pont De Nemours And Company Waterbased coating composition of methylol (meth)acrylamide acrylic polymer, acrylic hydrosol and melamine crosslinking agent
JP2004307850A (en) * 2003-03-25 2004-11-04 Nippon Paint Co Ltd Production process of internally cross-linked fine particle resin containing o/w type emulsion, cation electrodeposition coating composition and coated product
JP4523784B2 (en) * 2003-03-25 2010-08-11 日本ペイント株式会社 Method for producing fine resin particle-containing O / W emulsion, internally crosslinked fine resin particle-containing O / W emulsion, cationic electrodeposition coating composition and coated article

Also Published As

Publication number Publication date
JPS6031329B2 (en) 1985-07-22

Similar Documents

Publication Publication Date Title
TW528765B (en) Polymers, blends, and process for making articles
US5147907A (en) Process of producing aqueous polymer dispersions
Pi et al. Synthesis and characterization of low-temperature self-crosslinkable acrylic emulsion for PE film ink
Ghosh et al. Use of glycidyl methacrylate monomers for developing cross-linkable pressure sensitive adhesives
Zhang et al. Synthesis and characterization of crosslinkable latex with interpenetrating network structure based on polystyrene and polyacrylate
US5916963A (en) Water-based resin dispersion and process for the production thereof
CN108359047A (en) A kind of waterborne acrylic paint and preparation method thereof that graphene is modified
Meng et al. Synthesis, characterization and formation mechanism of acrylate emulsion-based self-matting coatings
JPS6086107A (en) Powdery tackifying and bonding agent gel-formable in gasoline and paint and coating containing same
JPS61264077A (en) Water-dispersed type pressure-sensitive adhesive composition
JPS5853940A (en) Preparation of hydrosol
CN115124657B (en) Acrylate emulsion with core-shell structure and preparation method thereof
Córdoba et al. Waterborne acrylic-melamine latexes with controlled film microstructure
JPH10182987A (en) Sliding resin composition
JPS58136647A (en) Production of hydrosol
JPH08501344A (en) Graft and core-shell copolymers with improved phase bonding between the graft substrate and the grafted polymer phase
JP3944890B2 (en) Undercoat agent for release paper
Chen et al. Study on influence of monobutyl itaconate and N, N-diethylacrylamide on acrylic latex
JPS58164632A (en) Production of hydrosol
JPS59184241A (en) Production of hydrosol
JPS58168602A (en) Production of hydrosol
JP2959796B2 (en) Water dispersible resin composition and method for producing the same
JPH04142312A (en) Highly crosslinked flexible bead polymer
JP2880748B2 (en) Latex composition
JPS6245885B2 (en)