JPH064810B2 - High solid type synthetic resin coating composition - Google Patents
High solid type synthetic resin coating compositionInfo
- Publication number
- JPH064810B2 JPH064810B2 JP12147185A JP12147185A JPH064810B2 JP H064810 B2 JPH064810 B2 JP H064810B2 JP 12147185 A JP12147185 A JP 12147185A JP 12147185 A JP12147185 A JP 12147185A JP H064810 B2 JPH064810 B2 JP H064810B2
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- monomer
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- resin
- vinyl chloride
- polymerization
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Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は安価な溶剤に溶解性の良い、ハイソリッド樹脂
溶液で、厚塗りが可能な塩化ビニル系樹脂塗料に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a vinyl chloride-based resin coating material which is highly soluble in an inexpensive solvent and can be applied thickly with a high solid resin solution.
塩化ビニル共重合体を主成分とする塩化ビニル系塗料は
耐薬品性,耐水性,耐候性が良好で塗り重ねが自由にで
きるため、鉄鋼やコンクリートによる構築物の塗装に広
く使用されている。Vinyl chloride-based paints containing vinyl chloride copolymer as the main component have good chemical resistance, water resistance and weather resistance, and can be applied over freely, so they are widely used for coating structures made of steel or concrete.
しかし、この種の塩化ビニル共重合体は、安価でかつ塗
料溶剤として好適なトルエン,キシレンなどの芳香族炭
化水素類あるいはエタノール,メタノールなどの脂肪族
アルコール類に本来不溶であるため、高価なケトン系ま
たはエステル系の溶剤、例えばメチルエチルケトン,メ
チルイソブチルケトン,酢酸エチル,酢酸ブチルなどを
必要とする。さらに溶液の樹脂濃度を高めると粘度が増
大し、かつ塗料化を行なう時、ゲル化を起し易い。この
ように溶解性の悪い樹脂塗料は溶剤で希釈して低濃度で
使用するため、厚膜を得るには、何回も重ね塗りしなけ
ればならず経済性および作業性に劣る欠点を有する。However, since this type of vinyl chloride copolymer is essentially insoluble in aromatic hydrocarbons such as toluene and xylene or aliphatic alcohols such as ethanol and methanol that are inexpensive and suitable as a coating solvent, it is expensive. A system- or ester-based solvent such as methyl ethyl ketone, methyl isobutyl ketone, ethyl acetate, butyl acetate or the like is required. Further, if the resin concentration of the solution is increased, the viscosity is increased, and gelation is likely to occur when it is made into a paint. Since such a resin paint having poor solubility is diluted with a solvent and used at a low concentration, it has to be repeatedly applied multiple times to obtain a thick film, which is disadvantageous in economical efficiency and workability.
この塩化ビニル系塗料の高濃度樹脂化についてはいくつ
かの文献がある。例えば特許公告昭47−28887に
よれば塩化ビニルとプロピオン酸ビニルとの共重合によ
り高濃度樹脂が得られ、芳香族炭化水素溶剤に溶解する
特性を有することを開示している。また、特許公告昭5
1−10,873には塩化ビニル,酢酸ビニルおよび2
−ヒドロキシアルキルアクリレート共重合体が他の樹脂
との相溶性に優れていることを開示しているが、高濃度
樹脂化するための溶解性は劣る。さらに、特許公告昭5
2−24,558によれば、塩化ビニル,飽和カルボン
酸のビニルエステルおよびヒドロキシアルキルアクリレ
ートの共重合による樹脂が他の樹脂との相溶性の良い高
固形分含量塗料と成り得ることを開示している。しか
し、塩化ビニル含量が約70〜90重量%と高い共重合
体であり、高濃度樹脂化は十分ではなく、トルエンやキ
シレン等の芳香族炭化水素類溶剤への溶解性に劣る。There are some documents regarding the high-concentration resinization of this vinyl chloride-based paint. For example, Japanese Patent Publication No. 47-28887 discloses that a high-concentration resin can be obtained by copolymerization of vinyl chloride and vinyl propionate and has a property of being dissolved in an aromatic hydrocarbon solvent. Also, the patent publication Sho 5
1-10, 873 include vinyl chloride, vinyl acetate and 2
-It is disclosed that the hydroxyalkyl acrylate copolymer has excellent compatibility with other resins, but the solubility for forming a high concentration resin is poor. Furthermore, the patent publication Sho 5
2-24,558 discloses that a resin obtained by copolymerizing vinyl chloride, a vinyl ester of a saturated carboxylic acid and a hydroxyalkyl acrylate can be a high solid content coating material having good compatibility with other resins. There is. However, since it is a copolymer having a high vinyl chloride content of about 70 to 90% by weight, it cannot be sufficiently converted into a high-concentration resin, and its solubility in an aromatic hydrocarbon solvent such as toluene or xylene is poor.
本発明の目的は、従来品の欠点、即ち厚塗りできない点
および安価な芳香族炭化水素類や脂肪族アルコール類溶
剤への溶解性の劣る欠点を改善した塩化ビニル共重合体
樹脂からなる塗料組成物を提供することにある。The object of the present invention is to improve the drawbacks of conventional products, that is, the inability to thickly coat and the poor solubility in inexpensive aromatic hydrocarbons and aliphatic alcohols, to a coating composition comprising a vinyl chloride copolymer resin. To provide things.
本発明における三元共重合体は高濃度樹脂化の点におい
て従来の共重合体よりも優れており、さらに各種溶剤へ
の溶解性も幅の広いものとなっており、特にメタノー
ル,エタノールなどの脂肪族アルコール類溶剤への溶解
性に効果が認められる。従来の塩化ビニル系樹脂では予
想できない、エタノールやメタノール等の脂肪族アルコ
ール類溶剤による希釈が可能である。The terpolymer of the present invention is superior to conventional copolymers in terms of high-concentration resinization, and has a wide range of solubility in various solvents, particularly methanol, ethanol, etc. It has an effect on the solubility in aliphatic alcohol solvents. Dilution with an aliphatic alcohol solvent such as ethanol or methanol, which cannot be expected with conventional vinyl chloride resins, is possible.
即ち、本発明は(a)塩化ビニル単量体50〜69重量
%,(b)プロピオン酸ビニル単量体16〜40重量%,
(c)アクリル酸またはメタクリル酸のグリコールモノエ
ステル単量体2〜20重量%からなる単量体類を有機溶
媒下でランダム共重合した重合度100〜600の共重
合体,有機溶剤,顔料、さらに目的に応じて添加される
補助剤から成る高相溶性ハイソリッド型塗料組成物にあ
る。That is, the present invention comprises (a) vinyl chloride monomer 50 to 69% by weight, (b) vinyl propionate monomer 16 to 40% by weight,
(c) A copolymer having a degree of polymerization of 100 to 600 obtained by randomly copolymerizing monomers consisting of 2 to 20% by weight of a glycol monoester monomer of acrylic acid or methacrylic acid in an organic solvent, an organic solvent, a pigment, Further, it is a highly compatible high solid type coating composition comprising an auxiliary agent added according to the purpose.
本発明において用いられる塩化ビニル共重合体樹脂のラ
ンダム性は高濃度樹脂化および各種溶剤への溶解性を良
くするために重要である。ランダム性の高い共重合体を
得るためには重合系内の単量体組成分布が常に均一にな
るような方法で実施されればよく、例えば次のような方
法によって製造することができる。即ち、重合系内に一
定の単量体組成比を維持するように各単量体を、その各
々の重合速度に応じて供給することにより、言いかえる
と、重合体への単量体の転化率に等しい割合で供給する
ことにより、共重合体の単量体組成分布をより均一とす
る。The randomness of the vinyl chloride copolymer resin used in the present invention is important for achieving high-concentration resin and improving the solubility in various solvents. In order to obtain a copolymer having high randomness, it may be carried out by a method such that the monomer composition distribution in the polymerization system is always uniform, and for example, it can be produced by the following method. That is, by supplying each monomer so as to maintain a constant monomer composition ratio in the polymerization system, depending on the respective polymerization rate, in other words, conversion of the monomer into a polymer. By supplying at a rate equal to the rate, the monomer composition distribution of the copolymer becomes more uniform.
本出願人の特開昭61−278512号「塩化ビニル共
重合体の製造法」に記載された方法を特に好ましい方法
として挙げることができる。The method described in Japanese Patent Application Laid-Open No. 61-278512 “Method for producing vinyl chloride copolymer” by the present applicant can be mentioned as a particularly preferable method.
共重合は溶液状態で実施される。溶剤としてはエステル
類例えば酢酸エチル,酢酸ブチル;ケトン類例えばメチ
ルエチルケトン,メチルイソブチルケトン;芳香族炭化
水素類例えばトルエン,キシレン;などの単独あるいは
混合物が用いられる。重合における溶剤量対単量体量の
比は得られる樹脂溶液の粘度が低いため約3:7〜5:
5の間で使用できる。溶剤量/単量体量比の大きい所で
も重合は可能であるが、生産性が悪く樹脂分当りの価格
も高くなるので好ましくない。重合容器に単量体,溶剤
および重合開始剤を仕込み、所定の温度で重合を開始す
る。使用する温度,単量体対溶剤比および溶剤の種類の
組合せによって樹脂の分子量が制御される。重合度(J
IS K−6721,0.2g試料/50mニトロベ
ンゼン30℃測定)は100〜600、好ましくは20
0〜500のものが用いられる。重合開始剤は遊離基を
熱的に発生する油溶性化合物、例えばジベンゾイルペル
オキシド,ジラウロイルペルオキシド,ジアセチルペル
オキシド,アゾビス(イソブチロニトリル),イソプロ
ピルペルオキシジカーボネート等のいづれも用いること
ができる。The copolymerization is carried out in solution. As the solvent, one or a mixture of esters such as ethyl acetate and butyl acetate; ketones such as methyl ethyl ketone and methyl isobutyl ketone; aromatic hydrocarbons such as toluene and xylene; and the like are used. The ratio of the amount of solvent to the amount of monomer in the polymerization is about 3: 7 to 5: because the viscosity of the resulting resin solution is low.
Can be used between 5 Polymerization is possible even in a place where the solvent / monomer ratio is large, but this is not preferable because the productivity is poor and the price per resin component is high. A polymerization vessel is charged with a monomer, a solvent and a polymerization initiator, and polymerization is started at a predetermined temperature. The combination of temperature, monomer-to-solvent ratio and solvent type used controls the molecular weight of the resin. Degree of polymerization (J
IS K-6721, 0.2 g sample / 50 m nitrobenzene at 30 ° C.) is 100 to 600, preferably 20.
The thing of 0-500 is used. As the polymerization initiator, any oil-soluble compound that thermally generates a free radical, such as dibenzoyl peroxide, dilauroyl peroxide, diacetyl peroxide, azobis (isobutyronitrile), or isopropyl peroxydicarbonate can be used.
塩化ビニル単量体は共重合体の重量を基にして50〜6
9重量%用いる。塩化ビニル単量体が50重量%未満で
あると塩化ビニル系塗料としての特性、すなわち耐薬品
性,耐水性,耐候性が劣る。また、70重量%を超える
と樹脂溶液の粘度が増大し、高濃度化が得られず、芳香
族炭化水素類などの安価な溶剤に対する溶解性も劣る。The vinyl chloride monomer is 50-6 based on the weight of the copolymer.
9% by weight is used. If the vinyl chloride monomer content is less than 50% by weight, the properties as a vinyl chloride-based paint, that is, chemical resistance, water resistance and weather resistance are poor. On the other hand, if it exceeds 70% by weight, the viscosity of the resin solution increases, a high concentration cannot be obtained, and the solubility in an inexpensive solvent such as aromatic hydrocarbons becomes poor.
また、プロピオン酸ビニル単量体は共重合体の重量を基
にして16〜40重量%用いる。プロピオン酸ビニル単
量体が16重量%未満であると、粘度低下が得られず、
芳香族炭化水素系の溶剤に対する溶解性も劣る。また4
0重量%を超えると塗膜の強度あるいは耐水性が低下す
る。The vinyl propionate monomer is used in an amount of 16 to 40% by weight based on the weight of the copolymer. If the vinyl propionate monomer is less than 16% by weight, the viscosity cannot be reduced,
Solubility in aromatic hydrocarbon solvents is also poor. Again 4
If it exceeds 0% by weight, the strength or water resistance of the coating film is lowered.
アクリル酸またはメタクリル酸のグリコールモノエステ
ル単量体としてはアクリル酸またはメタクリル酸とエチ
レングリコール,プロピレングリコール,ブタンジオー
ル,ペンタンジオール等のグリコールとのモノエステル
があげられる。本発明の特に重要な単量体はアクリル酸
またはメタクリル酸のエチレングリコールまたはプロピ
レングリコールモノエステルである。これらの単量体は
単独でまたは2種以上併せて、共重合体の重量を基にし
て2〜20重量%用いられる。2重量%未満では粘度の
低減化が不十分であり、脂肪族アルコール系溶剤による
希釈性が劣る。また、ヒドロキシル基を用いた硬化反
応、例えばイソシアネート含有ウレタンプレポリマーと
の硬化による優れた塗膜を得るには不十分である。20
重量%を超えると濁りの無い透明樹脂溶液を得るのは困
難であり、またこの単量体の増加は価格上昇をもたらす
点でも好ましくはない。Examples of glycol monoester monomers of acrylic acid or methacrylic acid include monoesters of acrylic acid or methacrylic acid with glycols such as ethylene glycol, propylene glycol, butanediol and pentanediol. Particularly important monomers of the present invention are ethylene glycol or propylene glycol monoesters of acrylic acid or methacrylic acid. These monomers are used alone or in combination of two or more, and used in an amount of 2 to 20% by weight based on the weight of the copolymer. If it is less than 2% by weight, the reduction of the viscosity is insufficient and the dilutability with the aliphatic alcohol solvent is poor. Further, it is insufficient for obtaining an excellent coating film by curing reaction using a hydroxyl group, for example, curing with an isocyanate-containing urethane prepolymer. 20
If it exceeds 5% by weight, it is difficult to obtain a transparent resin solution free from turbidity, and an increase in this monomer is not preferable also in that it causes an increase in price.
このようにして得られた塩化ビニル共重合体樹脂溶液は
有機溶剤,顔料さらに目的に応じて補助剤を加えて塗料
とする。The vinyl chloride copolymer resin solution thus obtained is added with an organic solvent, a pigment and, depending on the purpose, an auxiliary agent to form a paint.
以上の説明から明らかなように本発明によれば (1)同一溶剤の樹脂溶液において同一濃度の粘度が小さ
いため高濃度樹脂が得られ、一回の塗装による塗膜厚さ
が大であり、塗装の繰返し回数が減少し、作業性および
経済性にすぐれている。As apparent from the above description, according to the present invention, (1) a high-concentration resin is obtained because the viscosity of the same concentration in the resin solution of the same solvent is small, and the coating film thickness by one coating is large, The number of coating cycles is reduced, resulting in excellent workability and economy.
(2)安価なトルエン,キシレン,エチルベンゼンなどの
芳香族炭化水素類や、エタノール,メタノールなどの脂
肪族アルコール類などを溶剤として用いられるため経済
的に有利である。(2) It is economically advantageous because inexpensive aromatic hydrocarbons such as toluene, xylene, and ethylbenzene, and aliphatic alcohols such as ethanol and methanol are used as the solvent.
(3)共重合樹脂はヒドロキシル基を含有するため、尿素
−ホルムアルデヒド樹脂,メラミン−ホルムアルデヒド
樹脂,エポキシ樹脂あるいはイソシアネート含有ウレタ
ンプレポリマーと共反応させて優秀な硬化塗膜を形成す
ることができる。(3) Since the copolymer resin contains a hydroxyl group, it can be co-reacted with urea-formaldehyde resin, melamine-formaldehyde resin, epoxy resin or isocyanate-containing urethane prepolymer to form an excellent cured coating film.
(4)さらに、この共重合樹脂はランダム共重合体である
ため、ヒドロキシル基を含有した各種の重合体との相溶
性が大幅に向上する。(4) Furthermore, since this copolymer resin is a random copolymer, the compatibility with various polymers containing a hydroxyl group is significantly improved.
以下、実施例および比較例を挙げて本発明を具体的に説
明する。なお、例文中「部」とあるのは「重量部」を意
味する。Hereinafter, the present invention will be specifically described with reference to Examples and Comparative Examples. In the example sentence, "part" means "part by weight".
実施例1〜6 <塩化ビニル共重合樹脂の製造> 1の重合容器に表1の量の塩化ビニル単量体とプロピ
オン酸ビニル単量体を、さらに200部の酢酸エチルと
3部のジベンゾイルペルオキシドを仕込み、そして温度
を65℃に上昇させた。この重合容器に表1に示した量
のα,βエチレン式不飽和カルボン酸のグリコールモノ
エステルを6時間から10時間かけて連続的に供給し
た。重合終了後の樹脂は濁りのない透明溶液で、ゲル状
物は無かった。樹脂の平均重合度(JIS K 672
1による測定)を表1に示した。Examples 1 to 6 <Production of Vinyl Chloride Copolymer Resin> In a polymerization vessel of 1, the amounts of vinyl chloride monomer and vinyl propionate monomer shown in Table 1, 200 parts of ethyl acetate and 3 parts of dibenzoyl were added. Peroxide was charged and the temperature was raised to 65 ° C. To the polymerization vessel, the glycol monoester of α, β ethylenically unsaturated carboxylic acid shown in Table 1 was continuously fed over 6 to 10 hours. The resin after the polymerization was a clear solution with no turbidity and had no gel. Average degree of polymerization of resin (JIS K 672
1) is shown in Table 1.
比較例1 実施例1に準じてプロピオン酸ビニルの代りに酢酸ビニ
ルを使用して繰返した。濁りの無い透明溶液が得られ、
平均重合度は250であった。 Comparative Example 1 The procedure of Example 1 was repeated except that vinyl acetate was used instead of vinyl propionate. A clear solution with no turbidity is obtained,
The average degree of polymerization was 250.
比較例2 実施例1〜6と同様の重合容器に180部の塩化ビニ
ル,120部のプロピオン酸ビニル,200部の酢酸エ
チルおよび3部のジベンゾイルペルオキシドを仕込み、
そして温度を65℃に上昇させ重合を行った。濁りの無
い透明溶液が得られ、平均重合度は300であった。Comparative Example 2 The same polymerization vessel as in Examples 1 to 6 was charged with 180 parts of vinyl chloride, 120 parts of vinyl propionate, 200 parts of ethyl acetate and 3 parts of dibenzoyl peroxide.
Then, the temperature was raised to 65 ° C. to carry out polymerization. A clear solution having no turbidity was obtained, and the average degree of polymerization was 300.
比較例3 重合容器に240部の塩化ビニル,30部のプロピオン
酸ビニル,200部の酢酸エチルおよび3部のジベンゾ
イルペルオキシドを仕込み、そして温度を65℃に上昇
させた。これに30部の2−ヒドロキシプロピルアクリ
レートを連続滴加させながら重合を行った。重合途中か
ら粘度が増加し、攪拌不能なゲルが生成した。Comparative Example 3 A polymerization vessel was charged with 240 parts of vinyl chloride, 30 parts of vinyl propionate, 200 parts of ethyl acetate and 3 parts of dibenzoyl peroxide, and the temperature was raised to 65 ° C. Polymerization was carried out while continuously adding 30 parts of 2-hydroxypropyl acrylate thereto. The viscosity increased during the polymerization, and a gel that could not be stirred was produced.
比較例4 比較例3の単量体量を、塩化ビニル180部,プロピオ
ン酸ビニル30部および2−ヒドロキシプロピルアクリ
レート90部に代え、繰返した。重合途中から白濁し、
ゲルが生じた。Comparative Example 4 The amount of monomer in Comparative Example 3 was replaced with 180 parts of vinyl chloride, 30 parts of vinyl propionate, and 90 parts of 2-hydroxypropyl acrylate, and this was repeated. It becomes cloudy during the polymerization,
A gel formed.
<樹脂の溶液粘度> 実施例1〜6および比較例1〜2の樹脂の50重量%酢
酸エチル溶液の粘度を表2に示した。<Solution Viscosity of Resin> Table 2 shows the viscosities of the 50 wt% ethyl acetate solutions of the resins of Examples 1 to 6 and Comparative Examples 1 and 2.
<溶剤による希釈性> 実施例1および比較例1〜2の樹脂のn−ヘプタン,キ
シレンおよびエタノールによる希釈性を表3に示した。 <Dilutability with Solvent> Table 3 shows the dilutability of the resins of Example 1 and Comparative Examples 1 and 2 with n-heptane, xylene and ethanol.
試験法…樹脂をメチルイソブチルケトンの10重量%溶
液に調整した後、ビーカーに溶液を5gあるいは10g
計量した。溶液を攪拌しながら各溶剤を滴下し、下の新
聞紙の活字が見えなくなった点を終点とした。 Test method: After adjusting the resin to a 10 wt% solution of methyl isobutyl ketone, add 5 g or 10 g of the solution to a beaker.
Weighed. Each solvent was added dropwise while stirring the solution, and the point at which the type of the newspaper below could not be seen was taken as the end point.
<塗膜評価> 実施例1の樹脂に酸化チタン(石原産業:タイペークR
−820),安定剤(油化シェル:エピコート828)
およびシンナー(キシレン/メチルイソブチルケトン=
1/1)を配合し、固形分46.0重量%,粘度1,20
0センチポイズ(25℃)の塗料組成物を得た。塗膜性
能についてJISK−5400,K−5582に従って
試験を行なった結果充分合格することが確認された。<Evaluation of coating film> Titanium oxide was added to the resin of Example 1 (Ishihara Sangyo: Taipaque R).
-820), stabilizer (oiled shell: Epikote 828)
And thinner (xylene / methyl isobutyl ketone =
1/1), solid content 46.0% by weight, viscosity 1,20
A coating composition of 0 centipoise (25 ° C) was obtained. The coating film performance was tested according to JIS K-5400, K-5582, and it was confirmed that the film passed sufficiently.
また、比較例1の樹脂を同様に塗料化を行ない、塗料組
成物を得たが、粘度が3,300センチポイズ(25
℃)と高く、また顔料分散性が悪かった。Further, the resin of Comparative Example 1 was similarly made into a coating material to obtain a coating composition, which had a viscosity of 3,300 centipoise (25
℃) and the pigment dispersibility was poor.
<イソシアネート硬化塗膜> 実施例1および4の樹脂について、イソシアネートとの
硬化を調べた。イソシアネートとして、コロネートHL
(日本ポリウレタン製、NCO含量13%)をOH/NCO比が
1になるように配合し、塗膜を形成した。23℃,60
%RH恒温室に2週間放置後、引張試験(島津製作所:
オートグラフIS−5000型、引張速度10mm/mi
n)を行なった。<Isocyanate-cured coating film> The resins of Examples 1 and 4 were examined for curing with isocyanate. As an isocyanate, Coronate HL
(Nippon Polyurethane, NCO content 13%) was blended so that the OH / NCO ratio was 1 to form a coating film. 23 ° C, 60
% RH After being left in a temperature-controlled room for 2 weeks, tensile test (Shimadzu:
Autograph IS-5000 type, pulling speed 10mm / mi
n) was performed.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C08F 220:28) (56)参考文献 特開 昭61−278512(JP,A) 特開 昭61−126180(JP,A) 特開 昭60−206875(JP,A) 特公 昭52−50204(JP,B2)─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Office reference number FI technical display area C08F 220: 28) (56) References JP-A-61-278512 (JP, A) JP-A-61 -126180 (JP, A) JP-A-60-206875 (JP, A) JP-B-52-50204 (JP, B2)
Claims (2)
%,(b)プロピオン酸ビニル単量体16〜40重量
%,(c)アクリル酸またはメタクリル酸のグリコール
モノエステル単量体2〜20重量%からなる単量体類を
有機溶媒下でランダム共重合した重合度100〜600
の共重合体,有機溶剤,顔料さらに目的に応じて添加さ
れる補助剤から成るハイソリッド型合成樹脂塗料組成
物。1. A vinyl chloride monomer (a) 50 to 69% by weight, (b) vinyl propionate monomer 16 to 40% by weight, (c) acrylic acid or methacrylic acid glycol monoester monomer 2 Degree of polymerization of 100 to 600 by random copolymerization of monomers of 20 to 20% by weight in an organic solvent
High-solid type synthetic resin coating composition comprising the copolymer of 1., an organic solvent, a pigment and an auxiliary agent added according to the purpose.
ルモノエステル単量体がアクリル酸のエチレングリコー
ルモノエステルまたはプロピレングリコールモノエステ
ルあるいはメタアクリル酸のエチレングリコールモノエ
ステルまたはプロピレングリコールモノエステルである
特許請求の範囲第1項記載の塗料組成物。2. A glycol monoester monomer of acrylic acid or methacrylic acid is ethylene glycol monoester or propylene glycol monoester of acrylic acid or ethylene glycol monoester or propylene glycol monoester of methacrylic acid. The coating composition according to item 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12147185A JPH064810B2 (en) | 1985-06-06 | 1985-06-06 | High solid type synthetic resin coating composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12147185A JPH064810B2 (en) | 1985-06-06 | 1985-06-06 | High solid type synthetic resin coating composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61281164A JPS61281164A (en) | 1986-12-11 |
| JPH064810B2 true JPH064810B2 (en) | 1994-01-19 |
Family
ID=14811969
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12147185A Expired - Lifetime JPH064810B2 (en) | 1985-06-06 | 1985-06-06 | High solid type synthetic resin coating composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH064810B2 (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5250204B2 (en) | 2005-04-06 | 2013-07-31 | 株式会社日本触媒 | Particulate water-absorbing agent, absorber and absorbent article |
-
1985
- 1985-06-06 JP JP12147185A patent/JPH064810B2/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5250204B2 (en) | 2005-04-06 | 2013-07-31 | 株式会社日本触媒 | Particulate water-absorbing agent, absorber and absorbent article |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61281164A (en) | 1986-12-11 |
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