JPS6037801B2 - Method for producing vinyl resin water dispersion for coating - Google Patents

Method for producing vinyl resin water dispersion for coating

Info

Publication number
JPS6037801B2
JPS6037801B2 JP15903076A JP15903076A JPS6037801B2 JP S6037801 B2 JPS6037801 B2 JP S6037801B2 JP 15903076 A JP15903076 A JP 15903076A JP 15903076 A JP15903076 A JP 15903076A JP S6037801 B2 JPS6037801 B2 JP S6037801B2
Authority
JP
Japan
Prior art keywords
ethylenically unsaturated
parts
monomers
group
acid
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
Application number
JP15903076A
Other languages
Japanese (ja)
Other versions
JPS5380431A (en
Inventor
満 高橋
寿臣 中村
和彦 大谷
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.)
Nippon Paint Co Ltd
Original Assignee
Nippon Paint 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 Nippon Paint Co Ltd filed Critical Nippon Paint Co Ltd
Priority to JP15903076A priority Critical patent/JPS6037801B2/en
Publication of JPS5380431A publication Critical patent/JPS5380431A/en
Publication of JPS6037801B2 publication Critical patent/JPS6037801B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は、有機溶剤を添加した場合でも優れた貯蔵安定
性を示す被覆用ビニル系樹脂水分散体の製造方法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing an aqueous vinyl resin dispersion for coating that exhibits excellent storage stability even when an organic solvent is added.

従来、被覆用ビニル系樹脂水分散体の製造方法としては
、例えば特関昭51一7033号または48−6018
1号明細書に開示のカルボキシ官能性共重合体を乳化安
定剤として使用し、水中でエチレン性不飽和単量体を重
合する方法が知られている。
Conventionally, methods for producing vinyl resin aqueous dispersions for coating have been disclosed, for example, in Tokukan Sho 51-7033 or No. 48-6018.
It is known to polymerize ethylenically unsaturated monomers in water using the carboxy-functional copolymers disclosed in No. 1 as emulsion stabilizers.

しかし、この方法で得られる樹脂水分散体を塗料化する
場合、塗装作業性調節のため有機溶剤を添加すると、増
粘、凝集、沈澱等が起り易く、実用上極めて大きな問題
であった。本発明者らは、かかる問題点のない被覆用ビ
ニル系樹脂水分散体の製造方法を提供するため鋭意研究
を進めた結果、上記従来法の乳化安定剤として、a 一
般式、〔式中、R,およびR2は同一もしくは異なって
水素原子またはメチル基、R3は水素原子またはC,〜
3 のアルキル基、およびnは2〜20を表す。
However, when the aqueous resin dispersion obtained by this method is made into a paint, adding an organic solvent to adjust coating workability tends to cause thickening, aggregation, precipitation, etc., which is a very serious problem in practice. The present inventors have carried out extensive research in order to provide a method for producing an aqueous vinyl resin dispersion for coating without such problems, and as a result, as an emulsion stabilizer of the above conventional method, a general formula, [in the formula, R and R2 are the same or different and are a hydrogen atom or a methyl group, R3 is a hydrogen atom or C, ~
3 alkyl group, and n represents 2-20.

〕で示されるエチレン性不飽和単量体、b エチレン性
不飽和カルボン酸、およびc その他のエチレン性不飽
和単量体の重合により得られる、分子内に式、〔式中、
R,,R2,R3およびnは前記と同意義。
], b is an ethylenically unsaturated carboxylic acid, and c is another ethylenically unsaturated monomer obtained by the polymerization of an ethylenically unsaturated monomer having the formula [in the formula,
R,, R2, R3 and n have the same meanings as above.

〕で示される単位を特定比率で有し、且つ特定酸価のビ
ニル共重合体を中和したものを使用することにより、目
的とする樹脂水分散体が得られることを見出だした。本
発明は、かかる知見に基づいて完成されたもので、その
要旨は、上記エチレン性不飽和単量体a、エチレン性不
飽和カルボン酸bおよびその他のエチレン性不飽和単量
体cの重合により得られる、分子内に上記式〔ロ〕で示
される単位を5〜40%(重量%、以下同様)有し、且
つ酸価30〜200KOHの9′夕のビニル共重合体を
中和状態で存在下、エチレン性不飽和単量体を水性媒体
中で重合することを特徴とする被覆用ビニル系樹脂水分
散体の製造方法に存する。
] It has been discovered that the desired resin aqueous dispersion can be obtained by using a neutralized vinyl copolymer having a specific ratio of units represented by the formula and having a specific acid value. The present invention was completed based on this knowledge, and its gist is that the above ethylenically unsaturated monomer a, ethylenically unsaturated carboxylic acid b and other ethylenically unsaturated monomer c are polymerized. The obtained 9' vinyl copolymer having 5 to 40% (wt%, same hereinafter) of units represented by the above formula [B] in the molecule and having an acid value of 30 to 200 KOH is in a neutralized state. The present invention relates to a method for producing an aqueous vinyl resin dispersion for coating, which comprises polymerizing an ethylenically unsaturated monomer in an aqueous medium.

本発明における上記ビニル共重合体は、分子内に上記単
位を5〜40%、好ましくは10〜30%有し、且つそ
の酸価が30〜200KOH雌/夕、好ましくは35〜
150KOHの9/夕の範囲に設定されていることが重
要である。
The vinyl copolymer of the present invention has 5 to 40%, preferably 10 to 30%, of the above units in the molecule, and has an acid value of 30 to 200 KOH, preferably 35 to 30.
It is important that it is set in the 9/evening range of 150KOH.

上記単位の比率が5%未満であると、目的樹脂水分散体
の有機溶剤添加による貯蔵安定性が損なうことになり、
また40%を越えると、耐水性の低下を招く。上言己酸
価が30KOHの9/汐未満であると、当該ビニル共重
合体を中和して乳化安定剤として使用してもその乳化も
しくは分散機能が不充分となり、目的樹脂水分散体が安
定状態で得られなくなり、また200KOH収/夕を越
えると、目的樹脂水分散体の被膜物性、特に耐水性や耐
食性に悪影響を及ぼすことになり、実用的でない。本発
明で使用する上記ピニル共重合体は、エチレン性不飽和
単量体a5〜40%、当該ビニル共重合体の酸価が30
〜200KOH雌/夕となるよう配合されたエチレン性
不飽和カルボン酸b、およびその他のエチレン性不飽和
単量体cを、通常の方法で溶液重合することにより得ら
れる。
If the ratio of the above units is less than 5%, the storage stability of the target resin aqueous dispersion due to the addition of an organic solvent will be impaired.
Moreover, if it exceeds 40%, water resistance will deteriorate. As mentioned above, if the self-acid value is less than 9/Shi of 30KOH, even if the vinyl copolymer is neutralized and used as an emulsion stabilizer, its emulsifying or dispersing function will be insufficient, and the target resin aqueous dispersion will be If it cannot be obtained in a stable state, and if it exceeds 200 KOH yield/unit, it will adversely affect the physical properties of the target resin aqueous dispersion, especially the water resistance and corrosion resistance, and is not practical. The above-mentioned pinyl copolymer used in the present invention contains 5 to 40% ethylenically unsaturated monomer, and the vinyl copolymer has an acid value of 30%.
It is obtained by solution polymerizing an ethylenically unsaturated carboxylic acid (b) and other ethylenically unsaturated monomer (c) blended to have a concentration of ~200 KOH/h by a conventional method.

上記エチレン性不飽和単量体aとしては、例えばモノア
クリル酸ポリエチレングリコール、モノメタクリル酸ポ
リエチレングリコール、モノアクリル酸メトキシポリェ
チレングリコール、モノメタクリル酸メトキシポリェチ
レングリコール等が挙げられ、これらの1種または2種
以上の混合物で使用に供すればよい。
Examples of the ethylenically unsaturated monomer a include polyethylene glycol monoacrylate, polyethylene glycol monomethacrylate, methoxypolyethylene glycol monoacrylate, methoxypolyethylene glycol monomethacrylate, etc. It may be used as a seed or a mixture of two or more types.

上記エチレン性不飽和カルボン酸bとは、分子内に1個
のエチレン性不飽和基と1個以上のカルボキシル基を同
時に有する物質すべてを包含し、その具体例としては、
アクリル酸、メタクリル酸、クロトン酸、マレィン酸、
フマル酸、ィタコン酸、マレィン酸モノオクチル、マレ
ィン酸モノブチル、ィタコン酸モノオクチル、更にはメ
タクリル酸2ーヒドロキシェチルと無水フタル酸をモル
比1対1で付加した反応生成物等が挙げられ、これらの
1種または2種以上の混合物で使用に供すればよい。
The ethylenically unsaturated carboxylic acid b includes all substances that simultaneously have one ethylenically unsaturated group and one or more carboxyl groups in the molecule, and specific examples include:
Acrylic acid, methacrylic acid, crotonic acid, maleic acid,
Examples include fumaric acid, itaconic acid, monooctyl maleate, monobutyl maleate, monooctyl itaconate, and reaction products obtained by adding 2-hydroxyethyl methacrylate and phthalic anhydride in a molar ratio of 1:1. One or a mixture of two or more of these may be used.

上記他のエチレン性不飽和単量体cとしては、以下の群
({ィ}〜しり)から選ばれる1種または2種以上の混
合物が使用されてよい。
As the other ethylenically unsaturated monomer c, one or a mixture of two or more selected from the following groups may be used.

M アクリル酸またはメタクリル酸とC,〜,8のモノ
アルコールとのェステル(例えばアクリル酸エチル、ア
クリル酸n−ブチル、アクリル酸iーブチル、アクリル
酸2ーェチルヘキシル、メタクリル酸メチル、メタクリ
ル酸nーブチル、メタクリル酸iーブチル、メタクリル
酸ラウリル、メタクリル酸シクロヘキシル等)。
M Esters of acrylic acid or methacrylic acid and C, ~, 8 monoalcohols (e.g. ethyl acrylate, n-butyl acrylate, i-butyl acrylate, 2-ethylhexyl acrylate, methyl methacrylate, n-butyl methacrylate, methacrylate) (i-butyl methacrylate, lauryl methacrylate, cyclohexyl methacrylate, etc.)

かかる単量体は、被膜の光沢、透明性、機械的性質、耐
薬品性、耐候性、可裸性等を良好に保持するために使用
され、その使用量は全単量体中30%以上の範囲で選定
すればよい。(o’ヒドロキシル基含有エチレン性不飽
和単量体(例えばアクリル酸2−ヒドロキシヱチル、ア
クリル酸2ーヒドロキシプロピル、アクリル酸1−メチ
ル−2ーヒドロキシエチル、メタクリル酸2ーヒドロキ
シェチル、メタクリル酸1ーメチルーヒドロキシエチル
、モノメタクリル酸ポリプロピレングリコール、モノメ
タクリル酸グリセロール、メタクリル酸3ークロロー2
ーヒドロキシプロピル、アリルアルコール等)。
Such monomers are used to maintain good gloss, transparency, mechanical properties, chemical resistance, weather resistance, stripability, etc. of the coating, and the amount used is 30% or more of the total monomers. It is sufficient to select within the range of . (o' hydroxyl group-containing ethylenically unsaturated monomers (e.g. 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, 1-methyl-2-hydroxyethyl acrylate, 2-hydroxyethyl methacrylate, methacrylate) 1-methyl-hydroxyethyl acid, polypropylene glycol monomethacrylate, glycerol monomethacrylate, 3-chloro2 methacrylate
- hydroxypropyl, allyl alcohol, etc.).

かかる単量体は、乳化安定剤の安定化作用に寄与するが
、同時に目的樹脂水分散体に硬化剤が添加され、架橋被
膜を得たい場合において、上記単量体aおよびbだけで
は架橋密度が不充分の場合に、これを補なう目的で適量
使用される。し一 アルケニル芳香族単量体(例えばス
チレン、Q−メチルスチレン、クロロスチレン、ビニル
トルエン、パラターシヤリブチルスチレン等)。
Such monomers contribute to the stabilizing effect of the emulsion stabilizer, but when a curing agent is added to the target resin aqueous dispersion and it is desired to obtain a crosslinked film, monomers a and b alone do not have sufficient crosslink density. It is used in appropriate amounts to compensate for insufficient amounts. (1) Alkenyl aromatic monomers (eg, styrene, Q-methylstyrene, chlorostyrene, vinyltoluene, paratertiary butylstyrene, etc.).

かかる単量体は、被膜の光沢、透明性を改善するが、全
単量体中40%以下で使用することが望ましい。40%
を越えると、被膜の耐候性が劣ってくる。9 エチレン
性不飽和カルボン酸のアミドおよびその置換ァミド(例
えばアクリル酸ァミド、メタクリル酸アミド、マレィン
酸アミド、Nーメチロールアクリルアミド、Nーブトキ
シメチルアクリルアミド、ジアセトンアクリルアミド、
ヒドロキシメチルジアセトンアクリルアミド等)。
Such monomers improve the gloss and transparency of the coating, but it is desirable to use them in an amount of 40% or less of the total monomers. 40%
If it exceeds this, the weather resistance of the film will deteriorate. 9 Amides of ethylenically unsaturated carboxylic acids and their substituted amides (e.g. acrylic acid amide, methacrylic acid amide, maleic acid amide, N-methylolacrylamide, N-butoxymethylacrylamide, diacetone acrylamide,
hydroxymethyl diacetone acrylamide, etc.).

かかる単量体は、目的樹脂水分散体を自己架橋型とする
ことができ、その使用量は全単量体中30%以下の範囲
で選定すればよい。{対 エチレン性不飽和カルボン酸
のニトリル(例えばアクリロニトリル、メタクリロニト
リル等)。N エチレン性不飽和ジカルボン酸ジェステ
ル(例えばマレィン酸ジプチル等)。
Such a monomer can make the target resin aqueous dispersion self-crosslinking, and the amount used may be selected within a range of 30% or less based on the total monomers. {vs. Nitriles of ethylenically unsaturated carboxylic acids (e.g. acrylonitrile, methacrylonitrile, etc.). N Ethylenically unsaturated dicarboxylic acid gester (eg diptyl maleate, etc.).

(ト’アクリル酸グリシジルまたはメタクリル酸グリシ
ジルと脂肪酸との付加反応生成物。
(An addition reaction product between glycidyl acrylate or glycidyl methacrylate and fatty acids.

桝 アクリル酸またはメタクリル酸とェポキシ樹脂(シ
ェル社製商品名「カージュラE」)との付加反応生成物
An addition reaction product of acrylic acid or methacrylic acid and epoxy resin (trade name: "Cardura E" manufactured by Shell).

【リ} ブロックィソシアナート基含有エチレン性不飽
和単量体(例えばトリレンジィソシアナート、ィソホロ
ンジィソシアナート等のジィソシアナートの一方のィソ
シアナート基をラクタム、オキシム等のブロック剤でブ
ロックし、他方のィソシアナート基にメタクリル酸2−
ヒドロキシェチル等の活性水素基含有ヱチレン性不飽和
単量体を付加せしめた化合物等)。
[Li} Blocked isocyanate group-containing ethylenically unsaturated monomer (for example, diisocyanate such as tolylene diisocyanate, isophorone diisocyanate, etc.). One isocyanate group is blocked with a blocking agent such as lactam or oxime, and the other is methacrylic acid 2- to the isocyanate group of
Compounds to which ethylenically unsaturated monomers containing active hydrogen groups such as hydroxyethyl are added).

かかる単量体も、上託けの単量体と同様な機能を有し、
全単量体中30%以下の範囲で使用すればよい。肉 リ
ン酸基またはスルホン酸基含有エチレン性不飽和単量体
(例えばアシツドホスホオキシエチルメタクリレート、
3−クロロー2ーアシツドホスホオキシプロピルメタク
リレート、スルホン酸エチルメタクリレート、2ーアク
リルアミドー2−メチルプロパンスルホン酸等)。
Such monomers also have the same functions as the superconducting monomers,
It may be used in an amount of 30% or less of the total monomers. Meat Ethylenically unsaturated monomers containing phosphate or sulfonic acid groups (e.g. acid phosphooxyethyl methacrylate,
3-chloro 2-acid phosphooxypropyl methacrylate, ethyl sulfonate methacrylate, 2-acrylamido 2-methylpropanesulfonic acid, etc.).

かかる単量体は、乳化安定作用を付与することもできる
が、特に硬化促進のために全単量体中3%以下の範囲で
使用することが望ましい。妙 その他として塩化ビニル
、塩化ビニリデン、酢酸ビニル、エチレン等。
Although such monomers can also impart an emulsion stabilizing effect, it is desirable to use them in an amount of 3% or less based on the total monomers, particularly in order to accelerate curing. Other examples include vinyl chloride, vinylidene chloride, vinyl acetate, and ethylene.

上記溶液重合にあっては、通常の条件に従って実施され
てよく、例えばある重合温度に設定した適当な溶媒(例
えばジヱチレングリコールモノブチルェーテル)中、上
記所定割合の単量体a〜cを一括混合してバッチ式で反
応させるか、または連続滴下式で反応させればよい。
The above solution polymerization may be carried out according to usual conditions, for example, monomers a to (c) may be mixed all at once and reacted in a batch manner, or may be reacted in a continuous dropwise manner.

重合温度としては50〜150oo、重合時間は1〜1
彼時間が採用されてよい。かかる溶液重合によって、当
該ビニル共重合体を含む溶液系が得られ、このまま使用
に供すればよいoなお、本発明にあって、‐当該ビニル
共重合体の二次転移温度が40oo以下、好ましくは2
5qo以下に設定されている場合、目的樹脂水分散体を
塗料化し、これを塗装する時、湿度の影響が顕著に少な
くなる。
Polymerization temperature is 50~150oo, polymerization time is 1~1
He may take his time. Through such solution polymerization, a solution system containing the vinyl copolymer is obtained, and it can be used as is. is 2
If it is set to 5 qo or less, the influence of humidity will be significantly reduced when the target resin aqueous dispersion is made into a paint and this is painted.

即ち、低湿度時のドライスプレー、高温度時のタレが少
なくなり、また被塗物の表面状態の違いによる塗装ムラ
も少なくなる。特に、メタリック塗装に効果が大きい。
本発明に係る被覆用ビニル系樹脂水分散体は、上記酸価
30〜200KOHの9/夕のビニル共重合体を適当な
剤で中和した状態で存在下、各種のエチレン性不飽和単
量体を水性媒体中で重合(以下、乳化重合と称す)する
ことにより製造される。
That is, dry spraying at low humidity and sagging at high temperature are reduced, and coating unevenness due to differences in the surface condition of the object to be coated is also reduced. Particularly effective for metallic paint.
The vinyl resin aqueous dispersion for coating according to the present invention is prepared by adding various ethylenically unsaturated monomers in the presence of the above-mentioned vinyl copolymer having an acid value of 30 to 200 KOH and neutralized with an appropriate agent. It is produced by polymerizing the body in an aqueous medium (hereinafter referred to as emulsion polymerization).

上記ビニル共重合体は、それ自体乳化安定作用を有する
が、重合系に供するにはそのカルボキシル基の一部もし
くは全部を中和して水中に溶解または分散こなければな
らない。この中和処理は、重合系に供する前に完了させ
ておく必要はなく、当該ビニル共重合体と中和剤とを併
用して供しても達成される。上記中和剤としては、通常
のものが使用されてよく、例えばアルカリ性無機化合物
(水酸化カリウム、水酸化ナトリウム、炭酸カリウムな
ど)、および有機ァミン類(モノメチルアミン、ジメチ
ルアミン、トリメチルミン、モノエチルアミン、ジエチ
ルアミン、トリエチルアミン、モノプロピルアミン、ジ
メチルプロピルアミン等で代表される水溶性アミン類、
モノェタノールアミン、ジェタノールアミン、トリヱタ
ノールアミン、Nーメチルエタノールアミン、N−アミ
ノエチルエタノールアミン、N−メチルジエタノールア
ミン、モノイソフ。
The vinyl copolymer itself has an emulsion stabilizing effect, but before it can be used in a polymerization system, it must neutralize some or all of its carboxyl groups and dissolve or disperse it in water. This neutralization treatment does not need to be completed before being subjected to the polymerization system, and can be achieved by using the vinyl copolymer and a neutralizing agent together. As the neutralizing agent, usual ones may be used, such as alkaline inorganic compounds (potassium hydroxide, sodium hydroxide, potassium carbonate, etc.) and organic amines (monomethylamine, dimethylamine, trimethylamine, monoethylamine, etc.). , water-soluble amines represented by diethylamine, triethylamine, monopropylamine, dimethylpropylamine, etc.
Monoethanolamine, jetanolamine, triethanolamine, N-methylethanolamine, N-aminoethylethanolamine, N-methyldiethanolamine, monoisof.

ロ′ぐノールアミン、ジイソプロ/fノールアミン、ト
リイソプロ/ぐノールアミン、モノブタノールアミン等
で代表される水溶性オキシムアミン類、エチレンジアミ
ン、ジェチレントリアミン等で代表される多価アミンな
ど)が挙げられ、これらの群から選ばれる1種または2
種以上の混合物で使用に供すればよい。上記乳化重合に
供されるエチレン性不飽和単星体としては、目的樹脂水
分散体の被膜性能および用途に応じて、当該ビニル共重
合体の合成に使用された単量体a〜cの中から任意に1
種または2種以上組合わせて採用されてよく、またこれ
らにグリシジル基含有エチレン性不飽和単量体(例えば
アクリル酸グリシジル、メタクリル酸グリシジル、アク
リル酸メチルグリシジル、メタクリル酸メチルグリシジ
ル等)やビニル基を2個以上有する不飽和単量体(例え
ばビニルスチレン、ブタジェン、ジアクリル酸ポリエチ
レングリコール等)が適当量添加されてもよい。
These include water-soluble oxime amines such as diisopro/f-nolamine, triisopro/gnolamine, monobutanolamine, etc., and polyhydric amines such as ethylenediamine and jethylenetriamine. 1 or 2 selected from the group
A mixture of more than one species may be used. The ethylenically unsaturated single star to be subjected to the emulsion polymerization may be selected from monomers a to c used in the synthesis of the vinyl copolymer, depending on the coating performance and application of the target resin aqueous dispersion. arbitrarily 1
These may be used as a species or in combination of two or more, and in addition to these, glycidyl group-containing ethylenically unsaturated monomers (for example, glycidyl acrylate, glycidyl methacrylate, methylglycidyl acrylate, methylglycidyl methacrylate, etc.) or vinyl groups may be used. An appropriate amount of an unsaturated monomer having two or more of (for example, vinylstyrene, butadiene, polyethylene glycol diacrylate, etc.) may be added.

かかる単量体が非官能性を有するものであれば、熱可塑
性の樹脂水分散体が得られ、一方官能性を有するもので
あれば、熱硬化性(または熱硬化に好適な)樹脂水分散
体が得られる。具体的な単量体の組合わせの一例は、以
下の通りである。【i’熱可塑性の場合: アクリル酸またはメタクリル酸とC,〜,8のモノアル
コールとのェステル、アルケニル芳香族単量体、エチレ
ン性不飽和カルボン酸のニトリル、およびその他の非官
能性単量体を主成分とする組合わせ。
If such monomers are non-functional, a thermoplastic aqueous resin dispersion is obtained, whereas if they are functional, a thermosetting (or suitable for thermosetting) resin aqueous dispersion is obtained. You get a body. An example of a specific monomer combination is as follows. [i'For thermoplastics: esters of acrylic or methacrylic acid with C, ~, 8 monoalcohols, alkenyl aromatic monomers, nitriles of ethylenically unsaturated carboxylic acids, and other non-functional monomers. A combination whose main component is the body.

(ii} 熱硬化性の場合: アクリル酸またはメタクリル酸とC,〜,8のモノアル
コールとのェステル30以上、ヒドロキシル基含有エチ
レン性不飽和単量体5〜40%、およびその他の単量体
0〜65%から成る組合わせ。
(ii) In the case of thermosetting: 30 or more esters of acrylic acid or methacrylic acid and C, ~, 8 monoalcohol, 5 to 40% of ethylenically unsaturated monomers containing hydroxyl groups, and other monomers A combination consisting of 0-65%.

なお、この場合ヒドロキシル基含有エチレン性不飽和単
量体が使用されるが、一般にかかる単量体は、水と混和
性を有し重合中水相に移行し、そこで重合され、水熔性
もしくは水分散性ポリマーとなり、水相中に溶解したり
または樹脂粒子表面に吸着したりする。そのため、該単
量体の樹脂粒子中に分配される量が減少し、有効な架橋
可能点が不足する。従って、得られる樹脂水分散体に架
橋剤を添加して焼付塗膜を形成しても、均一な架橋反応
が得られず耐溶剤性等に劣る傾向を示す。そこで、水に
対して比較的難溶性乃至非混和性のヒドロキシル基含有
エチレン性不飽和単量体を選択使用することが望ましい
。具体例としては、一般式、〔式中、R4およびR5は
同一もしくは異なって水素原子またはメチル基、R6は
C3〜6 のアルキレン基、並びにmはR6がC3,4
のアルキレン基の場合2〜10およびその他の場合1
〜5を表わす。
In this case, a hydroxyl group-containing ethylenically unsaturated monomer is used, but generally such a monomer is miscible with water and migrates to the aqueous phase during polymerization, where it is polymerized and becomes water-soluble or It becomes a water-dispersible polymer and dissolves in the water phase or adsorbs on the surface of resin particles. Therefore, the amount of the monomer distributed in the resin particles decreases, resulting in a shortage of effective crosslinkable points. Therefore, even if a crosslinking agent is added to the obtained aqueous resin dispersion to form a baked coating film, a uniform crosslinking reaction cannot be obtained and solvent resistance tends to be poor. Therefore, it is desirable to select and use a hydroxyl group-containing ethylenically unsaturated monomer that is relatively sparingly soluble or immiscible in water. Specific examples include the general formula, [wherein R4 and R5 are the same or different and are a hydrogen atom or a methyl group, R6 is a C3-6 alkylene group, and m is R6 is a C3,4
2 to 10 in the case of an alkylene group and 1 in other cases
- represents 5.

〕で示される単量体、メタアリルアルコール、ジメチロ
ールプロピオン酸とグリシジル基含有エチレン性不飽和
単量体との付加物、3ークロロー2ーヒドロキシプロピ
ルメタクリレート等が挙げられ、特に上記一股式〔m〕
で示される単量体が好適である。
], methalyl alcohol, adducts of dimethylolpropionic acid and glycidyl group-containing ethylenically unsaturated monomers, 3-chloro-2-hydroxypropyl methacrylate, etc. In particular, monomers of the above single-prong type [ m〕
Monomers represented by are preferred.

また、上記他の単量体としては、例えばアルケニル芳香
族単量体、エチレン性不飽和カルボン酸の置換ァミド、
ブロックィソシァナート基含有エチレン性不飽和単量体
、グリシジル基含有エチレン性不飽和単量体等が好適で
ある。
Examples of the other monomers include alkenyl aromatic monomers, substituted amides of ethylenically unsaturated carboxylic acids,
Ethylenically unsaturated monomers containing blocked isocyanate groups, ethylenically unsaturated monomers containing glycidyl groups, and the like are suitable.

上言己ァルケニル芳香族単量体を使用すると、被膜の光
沢、透明性の改善効果が達成され、通常全単量体中40
%以下で使用することが望ましい。
As mentioned above, when the alkenyl aromatic monomer is used, the effect of improving the gloss and transparency of the coating is achieved, and usually 40% of the total monomers are used.
It is desirable to use less than %.

40%を越えると、耐候性が低下する傾向にある。If it exceeds 40%, weather resistance tends to decrease.

上記エチレン性不飽和カルボン酸の置換アミドやブロッ
クィソシアナート基含有エチレン性不飽和単量体を使用
すると、目的樹脂水分散体を自己架橋型とすることがで
き、それぞれ全単量体中30%以下で使用すればよい。
上記グリシジル基含有エチレン性不飽和単量体を使用す
ると、一定の条件の下では乳化重合時そのグリシジル基
は当該ビニル共重合体のカルボキシル基と付加反応して
、乳化安定剤は、重合樹脂粒子に化学的に結合され、得
られる樹脂水分散体の安定性および被膜の透明性、機械
的強度、その他の性能等をより一層向上せしめる効果が
奏される。
When the above-mentioned substituted amides of ethylenically unsaturated carboxylic acids or ethylenically unsaturated monomers containing blocked isocyanate groups are used, the target resin aqueous dispersion can be made into a self-crosslinking type, and each contains 30% of the total monomers. % or less.
When the above-mentioned glycidyl group-containing ethylenically unsaturated monomer is used, under certain conditions, the glycidyl group undergoes an addition reaction with the carboxyl group of the vinyl copolymer during emulsion polymerization, and the emulsion stabilizer becomes a polymer resin particle. The effect of further improving the stability of the resulting aqueous resin dispersion, the transparency, mechanical strength, and other properties of the coating is produced.

これに対し、乳化重合時グリシジル基とカルボキシル基
が付加反応しないように工夫すれば、自己架橋型の樹脂
水分敬体が得られる。使用量は、その目的によって適宜
変化させればよく、即ち被膜改善等を目的とする場合は
グリシジル基がカルボキシル基に対して10モル%以下
となるように、そして自己架橋型を目的とする場合はグ
リシジル基がカルボキシル基に対して70〜120モル
%となるように選定すればよい。上記乳化重合にあって
は、上述の如く当該ビニル共重合体を中和状態にしたも
のが乳化安定剤として使用できることから、通常の乳化
剤や界面活性剤を使用しないこと以外は、公知のあらゆ
る乳化重合法が適用できる。
On the other hand, if measures are taken to prevent the addition reaction between glycidyl groups and carboxyl groups during emulsion polymerization, a self-crosslinking resin water derivative can be obtained. The amount used may be changed as appropriate depending on the purpose; that is, if the purpose is to improve the film, the glycidyl group should be 10 mol% or less with respect to the carboxyl group, and if the purpose is to create a self-crosslinking type may be selected so that the glycidyl group accounts for 70 to 120 mol% relative to the carboxyl group. In the above emulsion polymerization, since the vinyl copolymer in a neutralized state can be used as an emulsion stabilizer as described above, any known emulsion polymerization method can be used, except that ordinary emulsifiers and surfactants are not used. Polymerization method can be applied.

例えば、重合触媒の存在下重合温度に設定した水性媒体
(水またはこれに適当な親水性溶媒を加えたもの)中、
反応成分(具体的には当該ビニル共重合体、中和剤、エ
チレン性不飽和単量体)を一括混合してバッチ式で反応
させるか、または各反応成分を適当に配分して別々に連
続滴下して反応させればよい。重合温度としては0〜1
0000、好ましくは30〜9000、重合時間は1〜
1畑時間が採用されてよい。乳化重合に際し、当該乳化
安定剤の使用量は、それ自体被膜形成成分となりうるた
め、その乳化安定作用および被膜性能に応じて適宜決定
されてよく、通常重合に供するエチレン性不飽和単量体
全量に対して、5〜70%の範囲で選定すればよい。上
記重合触媒としては、例えば過硫酸カリウム、過硫酸ア
ンモニウム、過酸化水素、過炭酸ナトリウムなどの無機
過酸化物、過酸化ペンゾィル、ジーt−ブチルベルオキ
シドなどの有機過酸化物、2,2′ーアゾビスー2,4
ージメチルバレロニトリルなどのアゾ系化合物、更に過
酸化物をピロ亜硫酸カリウム、重亜硫酸ナトリウム、ト
リェタノールアミンなどの還元剤と組み合せたレドック
ス系触媒等が挙げられ、これらの1種または2種以上の
混合物で使用に供すればよい。
For example, in an aqueous medium (water or a suitable hydrophilic solvent) set at the polymerization temperature in the presence of a polymerization catalyst,
The reaction components (specifically, the vinyl copolymer, neutralizing agent, and ethylenically unsaturated monomer) can be mixed all at once and reacted batchwise, or each reaction component can be appropriately distributed and reacted separately and continuously. It may be added dropwise to react. The polymerization temperature is 0 to 1
0000, preferably 30-9000, polymerization time 1-9000
One field time may be adopted. During emulsion polymerization, the amount of the emulsion stabilizer used can itself be a film-forming component, so it may be determined appropriately depending on its emulsion stabilizing effect and film performance, and usually the total amount of ethylenically unsaturated monomers used for polymerization. It may be selected within the range of 5 to 70%. Examples of the polymerization catalyst include inorganic peroxides such as potassium persulfate, ammonium persulfate, hydrogen peroxide, and sodium percarbonate; organic peroxides such as penzoyl peroxide and di-t-butyl peroxide; 2,4
Examples include azo compounds such as -dimethylvaleronitrile, and redox catalysts in which peroxide is combined with reducing agents such as potassium pyrosulfite, sodium bisulfite, and triethanolamine. It may be used as a mixture.

使用量は、通常反応成分全量に対し、0.01〜5%の
範囲で選定すればよい。なお、この乳化重合に際し、必
要に応じてn−オクチルメルカプタン、t−ドデシルメ
ルカプタン等で代表されるメルカプタン類、ジイソプロ
ピルザントゲンジスルフイドで代表されるジスルフィド
類、ハロゲン化物等の通常の連鎖移動剤を用いてもよく
、またグラフト活性基を有しないまたは有するァルキド
樹脂、アクリル樹脂等の改質用樹脂、アミノプラスト樹
脂、多官能性ブロックィソシァナート等の硬化剤、顔料
等を配合して乳化重合を行うこともできる。
The amount used may be normally selected within the range of 0.01 to 5% based on the total amount of reaction components. In this emulsion polymerization, if necessary, a conventional chain transfer agent such as mercaptans such as n-octyl mercaptan and t-dodecyl mercaptan, disulfides such as diisopropylsantogen disulfide, and halides may be used. Alternatively, modifying resins such as alkyd resins and acrylic resins that do not have or have graft active groups, curing agents such as aminoplast resins and polyfunctional block isocyanates, and pigments may be blended. Emulsion polymerization can also be carried out.

以上の如くして製造されたビニル系樹脂水分散体は、所
期目的の塗料化に際し、適当な有機溶剤(アルコール類
、エーテル類など)を添加しても優れた貯蔵安定性を発
揮することができ、そして重合用単量体(エチレン性不
飽和単量体)の種類を組合わせることにより熱可塑型ま
たは熱硬化型の被覆に適用でき、そのままで、または必
要によりアミノプラスト樹脂、多官能性ブロックィソシ
ァナート、ェポキシ樹脂等の硬化剤、顔料、消泡剤、表
面調整剤等を添加、更に他の水性樹脂を混合して塗料化
すればよい。
The aqueous vinyl resin dispersion produced as described above exhibits excellent storage stability even when an appropriate organic solvent (alcohols, ethers, etc.) is added when it is made into a paint for the intended purpose. By combining the types of polymerization monomers (ethylenically unsaturated monomers), it can be applied to thermoplastic or thermosetting coatings, either as is or as needed with aminoplast resins, polyfunctional A curing agent such as a block isocyanate, an epoxy resin, a pigment, an antifoaming agent, a surface conditioner, etc. may be added, and other water-based resins may be added to form a paint.

塗装は通常用いられる方法、例えばスプレー塗装、浸濃
塗装、露着塗装、ロールコー夕−、はけ塗り等により実
施され、常温または加熱により乾燥硬化させることによ
り、各種の目的性能、例えば光沢、透明性、機械的強度
、耐水性、耐沸水性、耐蝕性、耐薬品性、(耐酸性、耐
アルカリ性)、耐溶剤性、耐汚染性、耐熱性、耐膜性等
に優れた塗膜を形成することができる。このことから、
本発明方法で得られるビニル系樹脂水分散体は、高級上
塗り塗料用として好適であるといえる。次に実施例、比
較例および参考例を挙げて本発明を具体的に説明する。
Coating is carried out by commonly used methods such as spray coating, immersion coating, decoating coating, roll coating, brush coating, etc., and is dried and cured at room temperature or by heating to achieve various desired properties such as gloss and transparency. Forms coatings with excellent properties such as strength, mechanical strength, water resistance, boiling water resistance, corrosion resistance, chemical resistance (acid resistance, alkali resistance), solvent resistance, stain resistance, heat resistance, film resistance, etc. can do. From this,
It can be said that the aqueous vinyl resin dispersion obtained by the method of the present invention is suitable for use in high-grade top coatings. Next, the present invention will be specifically explained by giving Examples, Comparative Examples, and Reference Examples.

なお、例文中「部」および「%」あるは「重量部」およ
び「重量%」を意味する。実施例 1 冷却器、不活性ガス導入管および縄梓機を具備した反応
器に、ジェチレングリコールモノブチルェーテル36.
$部、アクリル酸62.2部、モノメタクリル酸ポリエ
チレングリコール(エチレンオキサイド単位の繰返し数
(n):約5個)166.5部、2−アクリルアミドー
2一メチルプロパンスルホ4ン酸4.1部、メタクリル
酸メチル92部、メタクリル酸nープチル125.9部
、アクリル酸n−ブチル193.安部、スチレン276
部、t−ドデシルメルカプタン24.7部および2,2
′−アゾビスイソブチロニトリル12.3部を仕込み、
窒素ガス気流中婿拝しながら温度120℃で4時間反応
せしめピニル共重合体溶液を得る。
Note that "parts" and "%" in the example sentences mean "parts by weight" and "% by weight." Example 1 A reactor equipped with a condenser, an inert gas inlet pipe, and a rope strainer was charged with 36% of diethylene glycol monobutyl ether.
$ parts, 62.2 parts of acrylic acid, 166.5 parts of polyethylene glycol monomethacrylate (number of repeating ethylene oxide units (n): approximately 5), 4.1 parts of 2-acrylamido-2-methylpropanesulfonate 92 parts of methyl methacrylate, 125.9 parts of n-butyl methacrylate, 193 parts of n-butyl acrylate. Abe, Styrene 276
parts, 24.7 parts of t-dodecyl mercaptan and 2,2 parts
'-Add 12.3 parts of azobisisobutyronitrile,
Reaction was carried out at a temperature of 120° C. for 4 hours under a nitrogen gas stream to obtain a pinyl copolymer solution.

該溶液中の共重合体の醗価約5皿OH雌′夕、数平均分
子量約11000であった。かかる溶液を80qoに冷
却し、これにメタクリル酸2−ヒドロキシェチル149
.4部、N−プトキシメチルアクリルアミド186.5
部、メタクリル酸メチル216部、メタクリル酸n−ブ
チル108部、アクリル酸n−プチル96.1部および
スチレン324部を加0え均一溶液とし、室温に冷却し
た後更にジメチルエタノールアミン76‐$部、メラミ
ンーホルムアルデヒド樹脂(アメリカンシアナミド社製
商品名「サィメ−ル303」)50の郡および2,2′
−アゾビス−2,4−ジメチルバレロニトリル43.2
部を加えタ均一溶液(以下、A溶液と称す)とする。次
に、冷却器、不活性ガス導入管、縄梓機および滴下装置
を具備した反応器に、脱イオン水2850部を仕込み鷹
枠下温度7000に保持し、窒素ガス気流中これに上記
A溶液全量を3時間要して滴下する。滴下終了後同温度
で2時間反応させて、不癒発分46.5%、粘度(B型
粘度計使用、以下同様)65比psで乳白色の被覆用ビ
ニル系樹脂水分散体を得る。上記樹脂水分散体10碇誠
こ対し、ジェチレングリコールモノプチルェーテル5部
およびエタノール5部を添加し、40ooで1鞘時間貯
蔵したが、増粘、凝集等の変化はなく均一安定であった
The copolymer in the solution had a concentration of about 5 OH and a number average molecular weight of about 11,000. The solution was cooled to 80 qo, and 149 qo of 2-hydroxyethyl methacrylate was added to it.
.. 4 parts, N-ptoxymethylacrylamide 186.5
216 parts of methyl methacrylate, 108 parts of n-butyl methacrylate, 96.1 parts of n-butyl acrylate and 324 parts of styrene were added to make a homogeneous solution, and after cooling to room temperature, 76 parts of dimethylethanolamine was added. , melamine-formaldehyde resin (product name: Cymer 303, manufactured by American Cyanamid Co.) 50 groups and 2,2'
-azobis-2,4-dimethylvaleronitrile 43.2
A homogeneous solution (hereinafter referred to as solution A) is obtained. Next, 2850 parts of deionized water was charged into a reactor equipped with a cooler, an inert gas inlet pipe, a rope scaler, and a dropping device, and the temperature under the frame was maintained at 7000°C. The entire amount is added dropwise over a period of 3 hours. After the dropwise addition is completed, the mixture is reacted at the same temperature for 2 hours to obtain a milky-white aqueous vinyl resin dispersion for coating with an uncured content of 46.5% and a viscosity (using a B-type viscometer, the same applies hereinafter) of 65 ps. To 10 Makoto Ikari of the above resin aqueous dispersion, 5 parts of diethylene glycol monobutyl ether and 5 parts of ethanol were added and stored at 40 oo for 1 hour, but it remained uniform and stable with no changes such as thickening or aggregation. there were.

実施例 2実施例1と同じ反応器に、ジヱチレングリコ
ールモノブチルヱ−テル31.$郡、アクリル酸56.
7部実施例1と同じモノメタクリル酸ポリエチレングリ
コール76.4部、メタクリル酸2−ヒドロキシェチル
35部、2−アクリルァミドー2−メチループロパンス
ルホン酸3.8部、メタクリル酸メチル95.8部、メ
タクリル酸n−ブチル107.5部、アクリル酸n−ブ
チル199.5部、スチレン223.4部、t−ドデシ
ルメルカプタン22.6部および2,2′−アゾビスィ
ソブチロニトリル11.3部を仕込み、窒素ガス気流中
蝿拝しながら温度12000で4時間反応せしめビニル
共重合体溶液を得る。
Example 2 In the same reactor as in Example 1, 31. $ county, acrylic acid 56.
7 parts Same as Example 1 Polyethylene glycol monomethacrylate 76.4 parts, 2-hydroxyethyl methacrylate 35 parts, 2-acrylamido-2-methyl-propanesulfonic acid 3.8 parts, methyl methacrylate 95.8 parts 107.5 parts of n-butyl methacrylate, 199.5 parts of n-butyl acrylate, 223.4 parts of styrene, 22.6 parts of t-dodecylmercaptan, and 11.5 parts of 2,2'-azobisisobutyronitrile. 3 parts were charged and reacted at a temperature of 12,000 for 4 hours under nitrogen gas flow to obtain a vinyl copolymer solution.

該溶液中の共重合体の酸価約52.歌OHの9/夕、数
平均分子量約9400であった。かかる溶液を80qの
こ冷却し、これにモノメタクリル酸ポリプロピレングリ
コール(プロピレンオキサィド単位の繰返し数(m):
約4個)273.4部、Nーブトキシメチルアクリルァ
ミド199.5部、メタクリル酸グリシジル10.7部
、3−クロロー2ーアシッドホスホオキシプロピルメタ
クリレート4.8部、メタクリル酸メチル357.$部
、メタクリル酸nーブチル130.2部、アクリル酸n
−ブチル195.3部およびスチレン130.2部を加
え均一溶液とし、室温に冷却した後更に「サイメール3
03」40碇都、ジメチルェタノールアミン56.1部
および2,2′−アゾビス−2,4−ジメチルバレロニ
トリル39.1部を加え均一溶液(以下、B溶液と称す
)とする。次に、実施例1と同じ反応器に、脱イオン水
3322郡を仕込み蝉梓下温度70oCに保持し、窒素
ガス気流中これに上記B溶液全量を3時間要して滴下す
る。
The acid value of the copolymer in the solution is about 52. The number average molecular weight was about 9,400 on the evening of Uta OH on September 9th. This solution was cooled by 80q, and polypropylene glycol monomethacrylate (number of repeating propylene oxide units (m):
4 parts) 273.4 parts, N-butoxymethylacrylamide 199.5 parts, glycidyl methacrylate 10.7 parts, 3-chloro-2-acid phosphooxypropyl methacrylate 4.8 parts, methyl methacrylate 357. $ parts, n-butyl methacrylate 130.2 parts, acrylic acid n
- 195.3 parts of butyl and 130.2 parts of styrene were added to make a homogeneous solution, and after cooling to room temperature,
A homogeneous solution (hereinafter referred to as solution B) was prepared by adding 40 parts of dimethylethanolamine and 39.1 parts of 2,2'-azobis-2,4-dimethylvaleronitrile. Next, 3322 g of deionized water was charged into the same reactor as in Example 1, and the temperature was maintained at 70oC, and the entire amount of the above solution B was added dropwise thereto over a period of 3 hours in a nitrogen gas stream.

滴下終了後同温度で2時間反応させて、不揮発分43.
0%、粘度50比psで乳白色の被覆用ピニル系樹脂水
分散体を得る。上記樹脂水分散体10戊靴こ対し、ジェ
チレソグリコールモノブチルェーテル5部およびエタノ
ール5部を添加し、4000で1斑時間貯蔵した所、少
しの増粘が見られたが凝集は認められなかった。
After the dropwise addition was completed, the reaction was carried out at the same temperature for 2 hours, and the non-volatile content was 43.
A milky white aqueous dispersion of pinyl resin for coating is obtained with a viscosity of 0% and a viscosity of 50 ps. When 10 parts of the above resin aqueous dispersion were added with 5 parts of diethylene glycol monobutyl ether and 5 parts of ethanol and stored at 4000 °C for 1 hour, a slight increase in viscosity was observed, but no aggregation occurred. I was not able to admit.

実施例 3実施例1と同じ反応器に、エチレングリコ一
ルモノェチルェーテル3碇邦、アクリル酸38.3部、
実施例1と同じモノメタクリル酸ポリエチレングリコー
ル187.5部、2−アクリルアミドー2−メチループ
ロパンスルホン酸3.8部、メタクリル酸メチル205
.5部、メタクリル酸nーブチル75部、アクリル酸n
ーブチル127.5部、スチレン112.5部、t−ド
デシルメルカプタン22.5部および2,2′ーァゾビ
スィソブーチロニトリル11.3部を仕込み、窒素ガス
気流中擬拝しながらら温度12000で4時間反応せし
めビニル共重合体溶液を得る。
Example 3 In the same reactor as in Example 1, 3 parts of ethylene glycol monoethyl ether, 38.3 parts of acrylic acid,
Same as Example 1: 187.5 parts of polyethylene glycol monomethacrylate, 3.8 parts of 2-acrylamido-2-methyl-propanesulfonic acid, 205 parts of methyl methacrylate.
.. 5 parts, n-butyl methacrylate 75 parts, acrylic acid n
127.5 parts of -butyl, 112.5 parts of styrene, 22.5 parts of t-dodecyl mercaptan and 11.3 parts of 2,2'-azobisisobutyronitrile were charged, and the mixture was heated under a stream of nitrogen gas. A vinyl copolymer solution was obtained by reacting at a temperature of 12,000 for 4 hours.

該溶液中の共重合体の酸価約40KOH雌/夕、数平均
分子量約7100であった。かかる溶液を80ooに冷
却し、これに実施例2と同じモノメタクリル酸ポリプロ
ピレングリコール262.5部、Nーブトキシメチルア
クリルアミド175部、3−クロロー2ーアシツドホス
ホオキシブロピルメタクリレート12.3部、メタクリ
ル酸メチル437.5部、メタクリル酸nーフチル26
2.5部、アクリル酸nーブチル274.8部およびス
チレン35碇部を加え均一溶液とし、室温に冷却した後
更にジメチルェタノールアミン37.$部および2,2
′ーアゾビスー2,4ージメチルバレロニトリル52.
5部を加え均一溶液(以下、C溶液と称す)とする。次
に、実施例1と同じ反応器に、脱イオン水3886部を
仕込み櫨梓下温度7℃に保持し、窒素ガス気流中これに
上記C溶液全量を3時間要して滴下する。
The acid value of the copolymer in the solution was about 40 KOH, and the number average molecular weight was about 7,100. This solution was cooled to 80 oo, and to this were added 262.5 parts of polypropylene glycol monomethacrylate, the same as in Example 2, 175 parts of N-butoxymethylacrylamide, 12.3 parts of 3-chloro-2-acid phosphooxypropyl methacrylate, 437.5 parts of methyl methacrylate, 26 parts of n-phthyl methacrylate
2.5 parts of n-butyl acrylate, 274.8 parts of n-butyl acrylate, and 35 parts of styrene were added to make a homogeneous solution, and after cooling to room temperature, 37 parts of dimethylethanolamine was added. $ part and 2,2
'-Azobis-2,4-dimethylvaleronitrile52.
5 parts were added to form a homogeneous solution (hereinafter referred to as C solution). Next, 3886 parts of deionized water was charged into the same reactor as in Example 1, and the temperature was maintained at 7° C., and the entire amount of the above C solution was added dropwise thereto over a period of 3 hours in a nitrogen gas stream.

滴下終了後同温度で2時間反応させて、不揮発分42.
8%、粘度55比psで乳白色の被覆用ビニル系樹脂水
分散体を得る。上記樹脂水分散体10碇都1こ対し、ジ
ェチレングリコールモノブチルェーテル5部およびエタ
ノール5部を添加し、40qoで1既時間貯蔵した所、
増粘、凝集等の変化はなく均一安定であった。
After the dropwise addition was completed, the reaction was carried out at the same temperature for 2 hours, and the non-volatile content was 42.
A milky white aqueous vinyl resin dispersion for coating is obtained with a viscosity of 8% and a viscosity of 55 ps. 5 parts of diethylene glycol monobutyl ether and 5 parts of ethanol were added to 1 bottle of the above resin aqueous dispersion, and the mixture was stored at 40 qo for 1 hour.
It was uniform and stable, with no changes such as thickening or aggregation.

実施例 4実施例1と同じ反応器に、ジェチレソグリコ
ールモノブチルェーテル27部、アクリル酸39.2部
、実施例1と同じモノメタクリル酸ポリエチレングリコ
ール101.3部、アクリル酸2ーヒドロキシフ。
Example 4 Into the same reactor as in Example 1, 27 parts of diethylene glycol monobutyl ether, 39.2 parts of acrylic acid, 101.3 parts of polyethylene glycol monomethacrylate same as in Example 1, and 2-hydroxyl acrylic acid were added. .

ロピル33.8部、2−アクリルアミド−2−メチルー
プロパンスルホン酸3.4部、メタクリル酸メチル13
5部、メタクリル酸n−ブチル202.5部、アクリル
酸n−ブチル16庇部、スチレン101.3部、n−ド
デシルメルカプタン20.3部および2,2′−アゾビ
スィソブーチロニトリル10.1部を仕込み、窒素ガス
気流中櫨拝しながら温度12000で4時間反応せしめ
ビニル共重合体溶液を得る。該溶液中の英重合体の酸価
約4耶OHの9′夕、数平均分子量約6900であった
。かかる溶液を80℃に冷却し、これにモノメタクリル
酸1,6ーヘキサンジオール283.5部、3−クロロ
−2−アシッドホスホオキシプロピルメタクリレート1
1部、メタクリル酸メチル472.5部、メタクリル酸
n−ブチル256.7部、アクリル酸n−ブチル236
.3部およびスチレン315部を加え均一溶液とし、室
温に冷却した後更に「サィメール303」250部、ジ
メチルェタノールアミン48.5部および2,2−ァゾ
ビス−2,4ージメチルバレロニトリル47.3部を加
え均一溶液(以下、D溶液と称す)とする。次に、実施
例1と同じ反応器に、脱イオン水3395部を仕込み櫨
梓下温度70q0に保持し、窒素ガス気流中これに上記
D溶液全量を3時間要して滴下する。
Lopil 33.8 parts, 2-acrylamido-2-methyl-propanesulfonic acid 3.4 parts, methyl methacrylate 13
5 parts, 202.5 parts of n-butyl methacrylate, 16 parts of n-butyl acrylate, 101.3 parts of styrene, 20.3 parts of n-dodecylmercaptan, and 10 parts of 2,2'-azobisisobutyronitrile. A vinyl copolymer solution was obtained by charging 1 part of the copolymer and reacting it at a temperature of 12,000 for 4 hours under a nitrogen gas stream for 4 hours. The polymer in the solution had an acid value of about 40OH and a number average molecular weight of about 6,900. The solution was cooled to 80°C, and 283.5 parts of 1,6-hexanediol monomethacrylate and 1 part of 3-chloro-2-acid phosphooxypropyl methacrylate were added to the solution.
1 part, 472.5 parts of methyl methacrylate, 256.7 parts of n-butyl methacrylate, 236 parts of n-butyl acrylate
.. 3 parts and 315 parts of styrene were added to make a homogeneous solution, and after cooling to room temperature, 250 parts of Cymer 303, 48.5 parts of dimethylethanolamine, and 47.3 parts of 2,2-azobis-2,4-dimethylvaleronitrile were added. 1 part to form a homogeneous solution (hereinafter referred to as solution D). Next, 3395 parts of deionized water was charged into the same reactor as in Example 1, and the temperature was maintained at 70q0, and the entire amount of the above solution D was added dropwise thereto over a period of 3 hours in a nitrogen gas stream.

滴下終了後同温度で2時間反応させて、不揮発分43.
6%、粘度43比psで乳白色の被覆用ビニル系樹脂水
分散体を得る。上記樹脂水分散体10の部‘こ対し、ジ
ェチレングリコールモノブチルェーテル5部およびエタ
ノール5部を添加し、40ooで1曲時間貯蔵した所、
増粘、凝集等の変化はなく均一安定であった。
After the dropwise addition was completed, the reaction was carried out at the same temperature for 2 hours, and the non-volatile content was 43.
A milky white aqueous vinyl resin dispersion for coating is obtained with a viscosity of 6% and a viscosity of 43 ps. To 10 parts of the above resin water dispersion, 5 parts of diethylene glycol monobutyl ether and 5 parts of ethanol were added, and the mixture was stored at 40°C for 1 hour.
It was uniform and stable, with no changes such as thickening or aggregation.

実施例 5実施例1と同じ反応器に、ジヱチレングリコ
ールモノブチルェーテル20部、アクリル酸45部、モ
ノメタクリル酸ポリエチレングリコール(エチレンオキ
サィド単位の繰返し数(n):約9個)15碇部、2−
アクリルアミドー2−メチルプロパンスルホン酸2.5
部、メタクリル酸メチル15碇部、アクリル酸n−ブチ
ル52.5部、スチレン100部、n−ドデシルメルカ
プタン15部および2,2′ーアゾビスィソブチロニト
リル7.5部を仕込み、窒素ガス気流中擬拝しながら温
度12000で4時間反応せしめピニル共重合体溶液を
得る。
Example 5 In the same reactor as in Example 1, 20 parts of diethylene glycol monobutyl ether, 45 parts of acrylic acid, and polyethylene glycol monomethacrylate (number of repeating ethylene oxide units (n): approximately 9) ) 15 Ikaribe, 2-
Acrylamide 2-methylpropanesulfonic acid 2.5
15 parts of methyl methacrylate, 52.5 parts of n-butyl acrylate, 100 parts of styrene, 15 parts of n-dodecylmercaptan and 7.5 parts of 2,2'-azobisisobutyronitrile were charged, and nitrogen gas was added. Reaction was carried out at a temperature of 12,000 for 4 hours under air flow to obtain a pinyl copolymer solution.

該溶液中の共重合体の酸価約70KOHm9ノタ、数平
均分子量約8300であった。かかる溶液を80qoに
冷却し、これに実施例2と同じモノメタクリル酸ポリプ
ロピレングリコール40碇邦、メタクリル酸グリシジル
40部、3−クロロ−2−アシッドホスホオキシプロピ
ルメタクリレート14部、メタクリル酸メチル646部
、メタクリル酸n山ブチル20の郡、アクリル酸n−ブ
チル40碇郡およびスチレン30碇部を加え均一溶液と
し、室温に冷却した後更にジメチルヱタノールアミン5
5.6部およびペンゾィルバーオキサィド6碇郡を加え
均一溶液(以下、E溶液と称す)とする。次に、実施例
1と同じ反応器に、脱イオン水3563部を仕込み櫨梓
下温度70o0に保持し、窒素ガス気流中これに上記E
溶液全量を3時間要して滴下する。
The copolymer in the solution had an acid value of about 70 KOHm9 and a number average molecular weight of about 8,300. This solution was cooled to 80 qo, and to this were added 40 parts of the same polypropylene glycol monomethacrylate as in Example 2, 40 parts of glycidyl methacrylate, 14 parts of 3-chloro-2-acid phosphooxypropyl methacrylate, 646 parts of methyl methacrylate, 20 parts of n-butyl methacrylate, 40 parts of n-butyl acrylate and 30 parts of styrene were added to make a homogeneous solution, and after cooling to room temperature, 5 parts of dimethylethanolamine was added.
5.6 parts and 6 parts of Pennzoilver oxide were added to form a homogeneous solution (hereinafter referred to as solution E). Next, 3563 parts of deionized water was charged into the same reactor as in Example 1, and the temperature was maintained at 70o0, and the above-mentioned E
The entire solution was added dropwise over a period of 3 hours.

滴下終了後同温度で2時間反応させて、不揮発分41.
5%、粘度81比psで乳白色の被覆用ビニル系樹脂水
分敵体を得る。上記樹脂水分散体10坊都‘こ対し、ジ
ェチレングリコールモノブチルェーテル5部およびエタ
ノール5部を添加し、40q0で1曲時間貯蔵した所、
増粘、凝集等の変化はなく均一安定であった。
After the dropwise addition was completed, the reaction was carried out at the same temperature for 2 hours, and the non-volatile content was 41.
5% and a viscosity of 81 ps to obtain a milky-white coating vinyl resin moisture admixture. To 10 pieces of the above resin water dispersion, 5 parts of diethylene glycol monobutyl ether and 5 parts of ethanol were added, and the mixture was stored at 40q0 for 1 hour.
It was uniform and stable, with no changes such as thickening or aggregation.

実施例 6実施例1と同じ反応器に、エチレングリコ‐
ルモノェチルェーテル2碇部、アクリル酸64部、モノ
4メタクリル酸メトキシポリェチレングリコール(エ
チレンオキサィド単位の繰返し数(n):約5個)15
碇部、メタクリル酸メチル5碇部、アクリル酸nープチ
ル186部、スチレン50部、t−ドデシルメルカプタ
ン17.5部および2,2′−アゾビスィソブチロニト
リル7.5部を仕込み、窒素ガス気流中縄拝しながら温
度120℃で4時間反応せしめビニル共重合体溶液を得
る。
Example 6 In the same reactor as in Example 1, ethylene glyco-
2 parts of monoethyl ether, 64 parts of acrylic acid, methoxypolyethylene glycol mono-4 methacrylate (number of repeating ethylene oxide units (n): approximately 5) 15
Anchorage, 5 anchorages of methyl methacrylate, 186 parts of n-butyl acrylate, 50 parts of styrene, 17.5 parts of t-dodecylmercaptan and 7.5 parts of 2,2'-azobisisobutyronitrile were charged, and nitrogen gas was added. A vinyl copolymer solution was obtained by reacting at a temperature of 120° C. for 4 hours while blowing in an air stream.

該溶液中の共重合体の酸価約100KOHの9ノタ、数
平均分子量約6200であった。かかる溶液を8000
に冷却し、これにメタクリル酸グリシジル4$部、メタ
クリル酸メチル36の部、アクリル酸n−ブチル140
0部およびスチレン20礎郡を加え均一溶液とし、室温
に冷却した0後更にジメチルェタノールアミン79.1
部を加え均一溶液(以下、F溶液と称す)とする。次に
、実施例1と同じ反応器に、脱イオン水318戊部を仕
込み櫨梓下温度7000に保持し、窒素ガス気流中これ
に上記F溶液全量と、過硫酸アンモタン2戊部および脱
イオン水40庇都から成る混合物とを3時間要して同時
滴下する。
The copolymer in the solution had an acid value of about 100 KOH, 9 knots, and a number average molecular weight of about 6,200. 8000 ml of such solution
4 parts of glycidyl methacrylate, 36 parts of methyl methacrylate, and 140 parts of n-butyl acrylate.
0 parts and 20 parts of styrene were added to make a homogeneous solution, and after cooling to room temperature, 79.1 parts of dimethylethanolamine was added.
1 part to form a homogeneous solution (hereinafter referred to as F solution). Next, 318 parts of deionized water was charged into the same reactor as in Example 1, and the temperature was kept at 7000, and the entire amount of the above F solution, 2 parts of ammothane persulfate, and deionized water were added to the reactor in a nitrogen gas stream. A mixture consisting of 40 ml of water was added dropwise over a period of 3 hours.

滴下終了後同温度で2時間反応させて、不揮発分40.
9%、粘度21&psで乳白色の被覆用ビニル系樹脂水
分散体を得る。上記樹脂水分散体10戊都‘こ対し、ジ
ェチレングリコールモノプチルェーテル5部およびエタ
ノール5部を添加し、40℃で1斑時間貯蔵した所、増
粘、凝集等の変化はなく均一安定であった。
After the dropwise addition was completed, the reaction was carried out at the same temperature for 2 hours, and the non-volatile content was 40.
A milky-white aqueous vinyl resin dispersion for coating is obtained with a viscosity of 9% and a viscosity of 21&ps. To 10 pieces of the above resin water dispersion, 5 parts of diethylene glycol monobutyl ether and 5 parts of ethanol were added, and when stored at 40°C for 1 hour, it was uniform with no changes such as thickening or aggregation. It was stable.

比較例 1実施例1と同じ反応器に、ジェチレングリコ
ールモノブチルェーテル32部、アクリル酸72部、メ
タクリル酸2−ヒドロキシェチル96部、メタクリル酸
メチル240部、メタクリル酸n−ブチル192部、ア
クリル酸n−ブチル12礎郡、スチレン160部、t−
ドデシルメルカプタン21.6部および2,2−アゾビ
スィソブチロニトリル11.2部を仕込み、窒素ガス気
流中鷹拝しながら温度120ご0で4時間反応せしめビ
ニル共重合体溶液を得る。
Comparative Example 1 In the same reactor as in Example 1, 32 parts of diethylene glycol monobutyl ether, 72 parts of acrylic acid, 96 parts of 2-hydroxyethyl methacrylate, 240 parts of methyl methacrylate, and 192 parts of n-butyl methacrylate were added. parts, n-butyl acrylate 12 parts, styrene 160 parts, t-
21.6 parts of dodecyl mercaptan and 11.2 parts of 2,2-azobisisobutyronitrile were charged and reacted at a temperature of 120° C. for 4 hours under a nitrogen gas stream to obtain a vinyl copolymer solution.

該溶液中の共重合体の酸価約70KOHの9/夕、数平
均分子量8600であった。かかる溶液を80℃に冷却
し、これにメタクリル酸2ーヒドロキシェチル144部
、メタクリル酸メチル396部、メタクリル酸n−ブチ
ル24礎郭、アクリル酸nーブチル18礎郭およびスチ
レン24の都を加え均一溶液とし、室温に冷却した後更
に「サィメール303」50拍部、ジメチルエタノール
アミン8$部および2,2′ーアゾビス−2,4ージメ
チルバレロニトリル48部を加え均一溶液(以下、G溶
液と称す)とする。次に、実施例1を同じ反応器に、脱
イオン水3605部を仕込み凝梓下温度70q0に保持
し、窒素ガス気流中これに上記G溶液全量を3時間要し
て滴下する。
The copolymer in the solution had an acid value of about 70 KOH and a number average molecular weight of 8,600. The solution was cooled to 80°C, and 144 parts of 2-hydroxyethyl methacrylate, 396 parts of methyl methacrylate, 24 parts of n-butyl methacrylate, 18 parts of n-butyl acrylate, and 24 parts of styrene were added. After making a homogeneous solution and cooling it to room temperature, 50 parts of Cymer 303, 8 parts of dimethylethanolamine, and 48 parts of 2,2'-azobis-2,4-dimethylvaleronitrile were added to make a homogeneous solution (hereinafter referred to as G solution). ). Next, in the same reactor as in Example 1, 3605 parts of deionized water was charged, the pre-condensation temperature was maintained at 70q0, and the entire amount of the above G solution was added dropwise thereto over a period of 3 hours in a nitrogen gas stream.

滴下終了後同温度で2時間反応させて、不揮発分44.
1%、粘度46比psで乳白色の樹脂水分散体を得る。
上記樹脂水分散体10碇鰍こ対し、ジェチレングリコー
ルモノブチルェーテル5部およびエタノール5部を添加
し、4000で1斑時間貯蔵した所、著しく増粘が起っ
て一部ケーキ状を呈していた。
After the dropwise addition was completed, the reaction was carried out at the same temperature for 2 hours, and the non-volatile content was 44.
A milky white resin water dispersion is obtained with a viscosity of 1% and a viscosity of 46 ps.
When 5 parts of diethylene glycol monobutyl ether and 5 parts of ethanol were added to 10 pieces of the above resin water dispersion and stored at 4,000 ℃ for 1 hour, the viscosity increased significantly and some parts became cake-like. It was showing.

参考例 1実施例2または比較例1で得た樹脂水分散体
10花輪こ、ジエチレングリコールモノブチルエーテル
5部、エタノール5部およびアルミペースト7.5部を
添加し、充分に分散混合して塗料溶液を作成する。
Reference Example 1 10 parts of the resin aqueous dispersion obtained in Example 2 or Comparative Example 1, 5 parts of diethylene glycol monobutyl ether, 5 parts of ethanol and 7.5 parts of aluminum paste were added and thoroughly dispersed and mixed to form a coating solution. create.

次いで、かかる塗料溶液をフオードカップNo.4で3
栃砂となるように粘度調節した後、吐出量21比c/分
で噂霧塗装する。なお、被塗物は、鉄板に熱硬化性ァル
キド樹脂の硬化塗膜が塗布されたもので、■サンドペー
パーで水と共に研摩した部分、■サンドペーパーで水の
非存在下研磨した部分、および■研磨していない部分を
有している。また、塗装環境は温度2500、湿度50
,70,90%で、競付乾燥は7500で1び分間の予
備加熱した後150qoで3び分間焼付を行った。上記
塗装の結果、実施例2の樹脂水分散体を用いたものは、
被塗物の表面状態および湿度の違いによる影響が少なく
、全体として同様に良好なメタリック感を与え、メタル
ムラのない仕上り外観を呈していた。これに対し、比較
例1の樹脂水分散体を用いたものは、湿度70%におい
て、水の非存在下で研磨した部分が他の部分と異なって
見え、メタルムラ、塗装ムラとなっていた。
The paint solution was then poured into food cup no. 4 in 3
After adjusting the viscosity so that it becomes horse chestnut sand, spray coating is applied at a discharge rate of 21 c/min. The objects to be coated were iron plates coated with a cured coating film of thermosetting alkyd resin; ■ areas polished with sandpaper and water, ■ areas polished with sandpaper in the absence of water, and ■ It has unpolished parts. Also, the painting environment is temperature 2500 and humidity 50.
, 70, and 90%, and competitive drying was performed by preheating at 7500 for 1 minute and then baking at 150 qo for 3 minutes. As a result of the above coating, the one using the resin water dispersion of Example 2 was as follows:
It was less affected by differences in the surface condition and humidity of the object to be coated, gave the same good metallic feel as a whole, and exhibited a finished appearance with no metallic unevenness. On the other hand, in the case of using the resin water dispersion of Comparative Example 1, at a humidity of 70%, the parts polished in the absence of water looked different from other parts, resulting in metal unevenness and coating unevenness.

Claims (1)

【特許請求の範囲】 1 a 一般式 ▲数式、化学式、表等があります▼ 〔式中、R_1およびR_2は同一もしくは異なつて
水素原子またはメチル基、R_3は水素原子またはC_
1〜C_3のアルキル基、およびnは2〜20を表わす
。 〕で示されるエチレン性不飽和単量体、bエチレン性不
飽和カルボン酸、およびcその他のエチレン性不飽和単
量体の重合により得られる、分子内に式、▲数式、化学
式、表等があります▼ 〔式中、R_1,R_2,R_3およびnは前記と同
意義。 〕で示される単位を5〜40重量%有し、且つ酸化30
〜200KOHmg/gのビニル共重合体を中和状態で
存在下、エチレン性不飽和単量体を水性媒体中で重合す
ることを特徴とする被覆用ビニル系樹脂水分散体の製造
方法。 2 他のエチレン性不飽和単量体が、アクリル酸または
メタクリル酸とC_1〜_1_8のモノアルコールとの
エステル、ヒドロキシル基含有エチレン性不飽和単量体
、アルケニル芳香族単量体、エチレン性不飽和カルボン
酸のアミドおよびその置換アミド、エチレン性不飽和カ
ルボン酸のニトリル、エチレン性不飽和ジカルボン酸ジ
エステル、アクリル酸グリシジルまたはメタクリル酸グ
リシジルと脂肪酸との付加反応生成物、アクリル酸また
はメタクリル酸とエポキシ樹脂との付加反応生成物、ブ
ロツクイソシアナート基含有エチレン性不飽和単量体、
並びにリン酸基またはスルホン酸基含有エチレン性不飽
和単量体の群から選ばれる1種または2種以上の混合物
である上記第1項記載の方法。 3 水性媒体中の重合に供するエチレン性不飽和単量体
の組合わせが、アクリル酸またはメタクリル酸とC_1
〜_1_8のモノアルコールとのエステル、アルケニル
芳香族単量体、エチレン性不飽和カルボン酸のニトリル
、およびその他の非官能性単量体を主成分とするもので
ある上記第1項記載の方法。 4 水性媒体中の重合に供するエチレン性不飽和単量体
の組合わせが、アクリル酸またはメタクリル酸とC_1
〜_1_8のモノアルコールとのエステル30重量%以
上、ヒドロキシル基含有エチレン性不飽和単量体5〜4
0重量%、およびその他の単量体0〜65重量%から成
るものである上記第1項記載の方法。 5 ヒドロキシル基含有エチレン性不飽和単量体が、一
般式、▲数式、化学式、表等があります▼ 〔式中、R_4およびR_5は同一もしくは異なつて
水素原子またはメチル基、R_6はC_3〜_6のアル
キレン基、並びにmはR_6がC_3,_4のアルキレ
ン基の場合2〜10およびその他の場合1〜5を表す。 〕で示される単量体である上記第4項記載の方法。 6 他の単量体の1成分として、リン酸基またはスルホ
ン酸基含有エチレン性不飽和単量体を含む上記第4項記
載の方法。 7 リン酸基またはスルホン酸基含有エチレン性不飽和
単量体が、水に難溶または水に非混和性の単量体である
上記第6項記載の方法。
[Claims] 1 a General formula ▲ Numerical formula, chemical formula, table, etc. ▼ [In the formula, R_1 and R_2 are the same or different and are a hydrogen atom or a methyl group, and R_3 is a hydrogen atom or a C_
1 to C_3 alkyl group, and n represents 2 to 20. ], b. ethylenically unsaturated carboxylic acid, and c. other ethylenically unsaturated monomers. Yes▼ [In the formula, R_1, R_2, R_3 and n have the same meanings as above. ] has 5 to 40% by weight of units represented by
A method for producing an aqueous vinyl resin dispersion for coating, which comprises polymerizing an ethylenically unsaturated monomer in an aqueous medium in the presence of ~200 KOHmg/g of a vinyl copolymer in a neutralized state. 2. Other ethylenically unsaturated monomers include esters of acrylic acid or methacrylic acid and monoalcohols of C_1 to_1_8, hydroxyl group-containing ethylenically unsaturated monomers, alkenyl aromatic monomers, ethylenically unsaturated Amides of carboxylic acids and substituted amides thereof, nitriles of ethylenically unsaturated carboxylic acids, diesters of ethylenically unsaturated dicarboxylic acids, addition reaction products of glycidyl acrylate or glycidyl methacrylate with fatty acids, acrylic acid or methacrylic acid and epoxy resins addition reaction product with blocked isocyanate group-containing ethylenically unsaturated monomer,
and one or a mixture of two or more selected from the group of phosphoric acid group-containing or sulfonic acid group-containing ethylenically unsaturated monomers. 3 The combination of ethylenically unsaturated monomers subjected to polymerization in an aqueous medium is acrylic acid or methacrylic acid and C_1
The method according to item 1 above, wherein the main components are esters with monoalcohols of ~_1_8, alkenyl aromatic monomers, nitriles of ethylenically unsaturated carboxylic acids, and other non-functional monomers. 4 The combination of ethylenically unsaturated monomers subjected to polymerization in an aqueous medium is acrylic acid or methacrylic acid and C_1
~_1_8 ester with monoalcohol 30% by weight or more, hydroxyl group-containing ethylenically unsaturated monomer 5-4
0% by weight and 0 to 65% by weight of other monomers. 5 Hydroxyl group-containing ethylenically unsaturated monomers have general formulas, ▲mathematical formulas, chemical formulas, tables, etc.▼ [In the formula, R_4 and R_5 are the same or different and are hydrogen atoms or methyl groups, R_6 is C_3 to _6 The alkylene group and m represent 2 to 10 when R_6 is a C_3,_4 alkylene group, and 1 to 5 in other cases. ] The method according to the above item 4, which is a monomer represented by the following. 6. The method according to item 4 above, which comprises a phosphoric acid group- or sulfonic acid group-containing ethylenically unsaturated monomer as one component of the other monomers. 7. The method according to item 6 above, wherein the phosphoric acid group- or sulfonic acid group-containing ethylenically unsaturated monomer is a monomer that is sparingly soluble in water or immiscible in water.
JP15903076A 1976-12-27 1976-12-27 Method for producing vinyl resin water dispersion for coating Expired JPS6037801B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15903076A JPS6037801B2 (en) 1976-12-27 1976-12-27 Method for producing vinyl resin water dispersion for coating

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15903076A JPS6037801B2 (en) 1976-12-27 1976-12-27 Method for producing vinyl resin water dispersion for coating

Publications (2)

Publication Number Publication Date
JPS5380431A JPS5380431A (en) 1978-07-15
JPS6037801B2 true JPS6037801B2 (en) 1985-08-28

Family

ID=15684712

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15903076A Expired JPS6037801B2 (en) 1976-12-27 1976-12-27 Method for producing vinyl resin water dispersion for coating

Country Status (1)

Country Link
JP (1) JPS6037801B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56131653A (en) * 1980-03-19 1981-10-15 Dainippon Toryo Co Ltd Resin composition for paint
EP0038127B1 (en) * 1980-04-14 1984-10-17 Imperial Chemical Industries Plc Multi-layer coating process involving use of aqueous basecoat composition containing crosslinked polymer microparticles and having a pseudoplastic or thixotropic character
US4668730A (en) * 1985-08-05 1987-05-26 National Starch And Chemical Corp. Colloid stabilized latex adhesives
EP0670355A1 (en) * 1994-03-04 1995-09-06 Sartomer Company, Inc. Water-based curable and cured compositions and a method for adhering a coating or adhesive to a substrate

Also Published As

Publication number Publication date
JPS5380431A (en) 1978-07-15

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