JP2001163984A - Aqueous dispersion - Google Patents
Aqueous dispersionInfo
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- JP2001163984A JP2001163984A JP34415899A JP34415899A JP2001163984A JP 2001163984 A JP2001163984 A JP 2001163984A JP 34415899 A JP34415899 A JP 34415899A JP 34415899 A JP34415899 A JP 34415899A JP 2001163984 A JP2001163984 A JP 2001163984A
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- Japan
- Prior art keywords
- carboxylic acid
- aqueous dispersion
- modified
- polyolefin
- weight
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Abstract
(57)【要約】
【課題】 ポリオレフィン系樹脂の成型又はフイルムに
対し、塗料、インキ又は接着剤のプライマー用途として
優れた付着性、塗膜外観、耐溶剤性を有し、かつ柔軟性
の良好な塗膜を与える水性分散液の提供。
【解決手段】 塩素含有率が15〜35重量%であるカルボ
ン酸変性塩素化ポリオレフィンとカルボン酸変性エチレ
ン−酢酸ビニル共重合体を90/10〜10/90の比率である混
合物から成り、塩基性物質で中和し、非イオン界面活性
剤を使って、水に分散させた水性分散液。PROBLEM TO BE SOLVED: To have excellent adhesion, coating appearance, solvent resistance and excellent flexibility as a primer for paints, inks or adhesives to a polyolefin resin molding or film. To provide an aqueous dispersion which gives a good coating. The carboxylic acid-modified chlorinated polyolefin having a chlorine content of 15 to 35% by weight and a mixture of a carboxylic acid-modified ethylene-vinyl acetate copolymer in a ratio of 90/10 to 10/90 are used. An aqueous dispersion neutralized with a substance and dispersed in water using a nonionic surfactant.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ポリオレフィン系
樹脂、例えばポリプロピレン、ポリエチレン、エチレン
−酢酸ビニル共重合体などの保護又は美粧を目的に得ら
れる塗料用樹脂組成物、又は接着剤に関する水性分散液
に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an aqueous dispersion of a resin composition for a paint or an adhesive obtained for the purpose of protection or cosmetics of a polyolefin resin, for example, polypropylene, polyethylene, ethylene-vinyl acetate copolymer and the like. It is about.
【0002】[0002]
【従来の技術】従来、ポリプロピレン等のオレフィン系
樹脂は、化学的安定性が高く、廉価であり、物性のバラ
ンスに優れていて、リサイクルが可能である等の理由に
より、その使用量は自動車部品、家庭用電化製品、家庭
用雑貨類向け成型品を中心に年々増加している。しかし
ながら、オレフィン系樹脂は分子鎖中に極性基を含まな
いため、塗装されにくく、接着等が困難であるという欠
点を有している。このため、ポリプロピレン系の塗装や
接着の場合には、プライマー又はワンコートとして塩素
化ポリプロピレンを主成分とした樹脂を使用するのが一
般的である。しかし、塩素化ポリプロピレンはトルエン
・キシレン等の芳香族系有機溶媒を使うのが一般的であ
り、安全衛生・環境汚染面から問題があった。2. Description of the Related Art Conventionally, olefin resins such as polypropylene have been used in automobile parts because of their high chemical stability, low cost, excellent balance of physical properties, and recyclability. , And the number of products for household appliances and household goods is increasing year by year. However, since the olefin-based resin does not contain a polar group in the molecular chain, it has a drawback that it is difficult to be applied and that adhesion and the like are difficult. For this reason, in the case of polypropylene-based coating or bonding, it is common to use a resin containing chlorinated polypropylene as a main component as a primer or one coat. However, chlorinated polypropylene generally uses an aromatic organic solvent such as toluene or xylene, and has a problem in terms of safety and health and environmental pollution.
【0003】そこで、塩素化ポリプロピレンの水性分散
液を製造する試みがなされてきている。カルボキシル基
含有塩素化ポリオレフィンの水分散物(特公平8-600
9)、樹脂組成物エマルションの製造法(特許272703
2)、反応性界面活性剤の使用(特許2603173)等が提案
されている。[0003] Attempts have been made to produce aqueous dispersions of chlorinated polypropylene. Aqueous dispersion of carboxyl group-containing chlorinated polyolefin (JP-B8-600
9), a method for producing a resin composition emulsion (Patent 272703)
2) Use of a reactive surfactant (Patent No. 2603173) has been proposed.
【0004】近年、これら環境問題から特に自動車内装
用途では、水性化がさかんに検討されている。この場
合、求められる性能として、付着性のみならず柔軟性も
必要である。しかし、近年の自動車内装用塗料における
塗膜の柔軟性改善要求を満たすうえでも、柔軟性付与成
分が必要である。しかし、上記塩素化ポリプロピレン単
独の水性樹脂分散液はポリプロピレンへの密着性は良好
なものの柔軟性は改善できない。さらに、上記塩素化ポ
リプロピレン単独の水性樹脂分散液はポリプロピレン以
外への素材、特に靴に用いられているエチレン−酢酸ビ
ニル共重合(以下EVAと記す)への密着性は悪い。[0004] In recent years, due to these environmental problems, especially for automotive interior applications, the use of water has been actively studied. In this case, the required performance requires not only adhesion but also flexibility. However, in order to satisfy the recent demand for improving the flexibility of the coating film in automotive interior paints, a flexibility-imparting component is required. However, the aqueous resin dispersion of chlorinated polypropylene alone has good adhesion to polypropylene, but cannot improve flexibility. Further, the aqueous resin dispersion of the chlorinated polypropylene alone has poor adhesion to materials other than polypropylene, particularly ethylene-vinyl acetate copolymer (hereinafter referred to as EVA) used for shoes.
【0005】一方、EVA共重合体エマルションについ
ては、紙とOPPフイルム及び木材用の水系接着剤(特
開昭62-135583、特開平6-65550)等の発明があるがオレ
フィン用途には無い。また、ポリオレフィン基材に対す
る水系接着剤として、アクリル酸エステル系共重合体に
塩素化樹脂を混合した水系接着剤(特許2561495号)が
提案されているが、トルエン及びキシレン等の芳香族溶
媒を塩素化樹脂に対して2〜20重量倍添加しているため
完全な水系とは言いがたい。また、用いられている塩素
化樹脂が酸変性されていないために、接着剤用途のみ使
用可能であり、プライマーとして使用する場合には、上
塗り塗料との付着性が悪く実用上問題がある。On the other hand, EVA copolymer emulsions include inventions such as water-based adhesives for paper, OPP film and wood (Japanese Patent Application Laid-Open Nos. 62-135583 and 6-65550), but they are not used for olefins. Further, as an aqueous adhesive for a polyolefin substrate, an aqueous adhesive obtained by mixing a chlorinated resin with an acrylate copolymer (Patent No. 2561495) has been proposed, but an aromatic solvent such as toluene and xylene is used in chlorine. It is hard to say that it is a complete aqueous system because it is added 2 to 20 times by weight to the modified resin. Also, since the chlorinated resin used is not acid-modified, it can be used only for adhesives. When used as a primer, it has poor adhesion to the top coat and has a practical problem.
【0006】また、塩素化ポリオレフィンの水性分散液
及びEVA共重合体の水性分散液を混合した系について
は、水溶性ポリエチレンプライマー組成物(特開平4-35
1681)及びポリオレフィン用水系接着剤組成物及びプラ
イマー(特開平6-25628)が提案されている。しかし、
前者は水性分散液製造時に原料樹脂の溶解性をあげるた
め大量の芳香族溶媒を用いて水溶化した溶剤型ポリエチ
レンプライマーの提供であり、水系分散液とは言い難
い。[0006] Further, for a system in which an aqueous dispersion of a chlorinated polyolefin and an aqueous dispersion of an EVA copolymer are mixed, a water-soluble polyethylene primer composition (JP-A-4-35
1681) and a water-based adhesive composition for polyolefin and a primer (JP-A-6-25628). But,
The former is to provide a solvent-type polyethylene primer which is made water-soluble by using a large amount of an aromatic solvent in order to increase the solubility of a raw material resin during the production of an aqueous dispersion, and is hardly an aqueous dispersion.
【0007】一方、後者は、塩素化ポリオレフィン濃度
が5〜25%の界面活性剤溶液(成分1)を2〜50重量部調
製し、EVA共重合体エマルション50〜98重量部(成分
2)と混合している。したがって、成分1が少ない場合
には、ポリオレフィンへの接着性が劣り、一方成分1を
多く含む場合には、相対的に界面活性剤の量が多くなる
ため、プライマーとして使用した場合には耐水性に劣る
事は容易に類推できる。また、プライマーとして使用す
る場合、1,1,1−トリクロロエチレン等の塩素化溶媒で予備洗浄処
理を必要としており、工程上煩雑である。On the other hand, for the latter, 2 to 50 parts by weight of a surfactant solution (component 1) having a chlorinated polyolefin concentration of 5 to 25% is prepared, and 50 to 98 parts by weight of an EVA copolymer emulsion (component 2) are prepared. Mixed. Therefore, when the amount of the component 1 is small, the adhesion to the polyolefin is inferior. On the other hand, when the amount of the component 1 is large, the amount of the surfactant is relatively large. It can be easily analogized that it is inferior. In addition, when used as a primer, a preliminary washing treatment is required with a chlorinated solvent such as 1,1,1-trichloroethylene, which is complicated in the process.
【0008】[0008]
【発明が解決しようとする課題】本発明は、ポリオレフ
ィン系樹脂の成型又はフイルムに対し、塗料、インキ又
は接着剤のプライマー用途として優れた付着性、塗膜外
観、耐溶剤性を有し、かつ柔軟性の良好な塗膜を与える
水性分散液に関するものである。DISCLOSURE OF THE INVENTION The present invention has excellent adhesion, coating film appearance, solvent resistance to moldings or films of polyolefin resins as primers for paints, inks or adhesives, and The present invention relates to an aqueous dispersion which gives a coating film having good flexibility.
【0009】[0009]
【課題を解決するための手段】前記問題点を解決するた
め本発明者等は鋭意研究した結果、塩素含有率が15〜
35重量%である塩素化ポリオレフィンとエチレン−酢
酸ビニル共重合体を90/10〜10/90の混合比からなる水性
分散液により達成できる事を見出した。Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above problems, and as a result, have found that the chlorine content is 15 to 15%.
It has been found that a 35% by weight chlorinated polyolefin and ethylene-vinyl acetate copolymer can be achieved by an aqueous dispersion having a mixing ratio of 90/10 to 10/90.
【0010】即ち、塩素化ポリオレフィン成分として
は、塩素含有率が15〜35重量%である塩素化ポリオ
レフィンで、好ましくはカルボン酸変性されたもので、
酸価が10〜100、数平均分子量が2000〜40000である。一
方、エチレン−酢酸ビニル共重合体成分は、カルボン酸
変性されたものが好ましい。上記(A)カルボン酸変性
塩素化ポリオレフィンと(B)カルボン酸変性エチレン
−酢酸ビニル共重合体の混合物を塩基性物質で中和し、
非イオン界面活性剤を使って、水に分散させた水性分散
液は、ポリオレフィン系樹脂の成型物又はフイルムに対
し、塗料、インキ又は接着剤のプライマー用途として密
着性、柔軟性、塗膜外観の良好な塗膜を与える事を見い
だした。That is, the chlorinated polyolefin component is a chlorinated polyolefin having a chlorine content of 15 to 35% by weight, preferably a carboxylic acid-modified one.
The acid value is 10 to 100, and the number average molecular weight is 2,000 to 40,000. On the other hand, the ethylene-vinyl acetate copolymer component is preferably a carboxylic acid-modified component. Neutralizing a mixture of the (A) carboxylic acid-modified chlorinated polyolefin and (B) carboxylic acid-modified ethylene-vinyl acetate copolymer with a basic substance,
An aqueous dispersion dispersed in water using a nonionic surfactant can be used as a primer for paints, inks or adhesives on molded products or films of polyolefin resins to improve adhesion, flexibility and appearance of coatings. It has been found that it gives a good coating film.
【0011】[0011]
【発明の実施の形態】本発明で用いられる水性分散液
は、(A)カルボン酸変性塩素化ポリオレフィンと
(B)カルボン酸変性エチレン−酢酸ビニル共重合体の
混合物を主成分とする。以下に詳細に説明する。DETAILED DESCRIPTION OF THE INVENTION The aqueous dispersion used in the present invention contains, as a main component, a mixture of (A) a carboxylic acid-modified chlorinated polyolefin and (B) a carboxylic acid-modified ethylene-vinyl acetate copolymer. This will be described in detail below.
【0012】(A)カルボン酸変性塩素化ポリオレフィ
ンは、ポリオレフィンをクロロホルム等の塩素に不活性
な溶剤に溶解させ、塩素ガスを吹き込んで塩素化して得
られるもので、塩素化の前あるいは後に不飽和カルボン
酸又はその無水物をグラフト共重合する事により、カル
ボキシル基を導入することができる。(A) The carboxylic acid-modified chlorinated polyolefin is obtained by dissolving the polyolefin in a solvent inert to chlorine, such as chloroform, and chlorinating by blowing a chlorine gas. The olefin is unsaturated before or after chlorination. A carboxyl group can be introduced by graft copolymerizing a carboxylic acid or its anhydride.
【0013】ポリオレフィンとは、エチレン若しくはポ
リプロピレンの単独共重合体、又はエチレン若しくはプ
ロピレンのコモノマー、例えばブテン−1、ペンテン−
1、ヘキセン−1、ブテン−1、ヘプテン−1、オクテ
ン−1などの炭素数2以上、好ましくは2〜6のα−オ
レフィンコモノマーのランダム共重合体であり、ブロッ
ク共重合体よりはランダム共重合体の方が好ましい。ま
た、コモノマーを2種類以上共重合しても良い。The polyolefin is a homopolymer of ethylene or polypropylene, or a comonomer of ethylene or propylene, for example, butene-1, pentene-
1, hexene-1, butene-1, heptene-1, octene-1, etc., are random copolymers of α-olefin comonomers having 2 or more carbon atoms, preferably 2 to 6, and are more random copolymers than block copolymers. Polymers are preferred. Further, two or more comonomers may be copolymerized.
【0014】(A)カルボン酸変性塩素化ポリオレフィ
ンの塩素含有率は、15重量%未満では、融点、溶融粘度
が高すぎて水分散がうまく行えない。35重量%を越える
と基材への密着性が劣るようになる。好ましくは18〜28
重量%である。When the chlorine content of the carboxylic acid-modified chlorinated polyolefin (A) is less than 15% by weight, the melting point and the melt viscosity are too high, so that the water cannot be dispersed well. If it exceeds 35% by weight, the adhesion to the substrate will be poor. Preferably 18-28
% By weight.
【0015】カルボン酸変性ポリオレフィンとは、上記
ポリオレフィンをα、β−不飽和カルボン酸又はその無
水物でグラフト反応により変性を行ったポリオレフィン
である。The carboxylic acid-modified polyolefin is a polyolefin obtained by modifying the above polyolefin with an α, β-unsaturated carboxylic acid or its anhydride by a graft reaction.
【0016】(A)カルボン酸変性塩素化ポリオレフィ
ンの酸価は10〜100が好ましく、酸価が10未満では極性
材料への接着性が劣り、酸価が100を越えるとポリプロ
ピレンへの接着性が劣るようになる。(A) The acid value of the carboxylic acid-modified chlorinated polyolefin is preferably from 10 to 100. If the acid value is less than 10, the adhesion to polar materials is poor. If the acid value exceeds 100, the adhesion to polypropylene is poor. Become inferior.
【0017】ポリオレフィンの変性に用いられるα、β
−不飽和カルボン酸又はその無水物としては、例えばマ
レイン酸、フマル酸、イタコン酸、シトラコン酸、アリル
コハク酸、メサコン酸、アコニット酸及びこれらの酸無
水物等が挙げられる。この他、これらカルボン酸のエス
テルも挙げられる。これらのうち、酸無水物が好まし
い。ポリオレフィンにα、β−不飽和カルボン酸または
その無水物をグラフト共重合する方法は公知の方法(例
えば特許2019232号)で行えば良い。例えば、ポリオレ
フィンを融点以上に加熱溶融させてラジカル発生剤の存
在下でグラフト共重合させる方法によって行うのが好ま
しい。Α, β used for modification of polyolefin
-Examples of unsaturated carboxylic acids or anhydrides thereof include maleic acid, fumaric acid, itaconic acid, citraconic acid, allylsuccinic acid, mesaconic acid, aconitic acid, and acid anhydrides thereof. In addition, esters of these carboxylic acids are also included. Of these, acid anhydrides are preferred. The method of graft copolymerizing an α, β-unsaturated carboxylic acid or an anhydride thereof with a polyolefin may be performed by a known method (for example, Japanese Patent No. 2019232). For example, it is preferable to carry out the method by heating and melting a polyolefin above its melting point and graft copolymerizing in the presence of a radical generator.
【0018】また、α、β−不飽和カルボン酸またはそ
の無水物をグラフト共重合した塩素化ポリオレフィンの
数平均分子量は2000ないし40000が好ましく、2000未満
では凝集力が不足してポリオレフィン樹脂に対する密着
力が悪くなり、40000を越えると水に分散させる時の操
作性が悪くなり好ましくない。分子量をこの範囲に抑え
る為には、原料の分子量やグラフト反応を行う時の条件
を選択することで可能であり、また一旦原料の分子量を
下げた後グラフト反応を行うと言う方法でも可能であ
る。なお、数平均分子量はGPC(ゲルパーミエーショ
ンクロマトグラフィ)で測定することができる。The number average molecular weight of the chlorinated polyolefin obtained by graft copolymerization of an α, β-unsaturated carboxylic acid or its anhydride is preferably from 2,000 to 40,000. If it exceeds 40,000, the operability at the time of dispersing in water deteriorates, which is not preferable. In order to keep the molecular weight within this range, it is possible to select the molecular weight of the raw material and the conditions for performing the graft reaction, and it is also possible to perform the graft reaction after the molecular weight of the raw material is lowered once. . The number average molecular weight can be measured by GPC (gel permeation chromatography).
【0019】(B)カルボン酸変性エチレン−酢酸ビニ
ル共重合体は、公知の方法で製造できる。例えば、特開
平3-112836のようにEVAをトルエン又はキシレン等の
芳香族炭化水素類に溶解させ、メチルアルコール又はエ
チルアルコール等の低級アルコール等を加え、特定量の
水の存在下でアルカリアルコラート触媒を用いてケン化
反応させる。得られたケン化物を、不飽和カルボン酸又
はその酸無水物、例えばマレイン酸、フマル酸、イタコン
酸、シトラコン酸、アリルコハク酸、メサコン酸、アコ
ニット酸及びこれらの酸無水物等及びこれらカルボン酸
のエステルも挙げられ、これらとラジカル開始剤と共に
反応させる事により得る事ができる。(B) The carboxylic acid-modified ethylene-vinyl acetate copolymer can be produced by a known method. For example, as disclosed in JP-A-3-12836, EVA is dissolved in an aromatic hydrocarbon such as toluene or xylene, a lower alcohol such as methyl alcohol or ethyl alcohol is added, and an alkali alcoholate catalyst is added in the presence of a specific amount of water. And a saponification reaction. The resulting saponified product is an unsaturated carboxylic acid or an acid anhydride thereof, for example, maleic acid, fumaric acid, itaconic acid, citraconic acid, allyl succinic acid, mesaconic acid, aconitic acid and acid anhydrides of these and the like and these carboxylic acids Esters are also mentioned, and can be obtained by reacting them with a radical initiator.
【0020】(B)カルボン酸変性エチレン−酢酸ビニ
ル共重合体の酢酸ビニル含量は好ましくは5〜60重量%
で、酢酸ビニル含量が5重量%未満になると溶融しづら
いため製造上難しく、60重量%を越えるとオレフィン系
樹脂成型物、フイルムへの付着性が不十分である。酸価
は好ましくは1〜60が望ましく、1未満では水分散が難
しく、60を越えると耐水性が悪くなる。(B) The carboxylic acid-modified ethylene-vinyl acetate copolymer preferably has a vinyl acetate content of 5 to 60% by weight.
If the vinyl acetate content is less than 5% by weight, it is difficult to produce because of difficulty in melting, and if it exceeds 60% by weight, adhesion to an olefin resin molded product or film is insufficient. The acid value is preferably from 1 to 60, and if it is less than 1, it is difficult to disperse in water, and if it exceeds 60, the water resistance becomes poor.
【0021】本発明において、水性分散液は、特許2700
526記載のような公知の方法により得る事ができる。す
なわち、(A)カルボン酸変性塩素化ポリオレフィン又
は(B)カルボン酸変性エチレン−酢酸ビニル共重合体
を(A)/(B)=90/10〜10/90の割合で混合し、約10
0℃で溶融させ、非イオン界面活性剤及びカルボキシル
基に対して0.4〜1.5化学当量の塩基性物質を加えて溶融
混練し、溶融状態において、80〜98℃の水を加えて、W
/O型の分散体を形成させ、続いて水を加えながらこれ
をO/W型の分散体に転相させ、必要に応じて追加量の
水を添加することにより、本発明の水性分散体を得る事
ができる。In the present invention, the aqueous dispersion is disclosed in Patent 2700
It can be obtained by a known method as described in 526. That is, (A) a carboxylic acid-modified chlorinated polyolefin or (B) a carboxylic acid-modified ethylene-vinyl acetate copolymer is mixed at a ratio of (A) / (B) = 90/10 to 10/90, and about 10
0 ° C, melted and kneaded by adding 0.4 to 1.5 chemical equivalents of a basic substance to the nonionic surfactant and carboxyl group, and in a molten state, adding water at 80 to 98 ° C,
An aqueous dispersion of the present invention is formed by forming a dispersion of the / O type and subsequently inverting this phase to an O / W type dispersion with the addition of water and, if necessary, adding an additional amount of water. Can be obtained.
【0022】また、二軸押出機を用いて、(A)/(B)=90
/10〜90/10の割合で混合し溶融混練した後、非イオン界
面活性剤及び塩基性物質を加えて溶融混練した後、水を
加えてW/OからO/Wへ転相させることにより、本発
明の水性分散体を得る事ができる。(A) / (B) = 90 using a twin-screw extruder.
After mixing and melt-kneading at a ratio of / 10 to 90/10, a nonionic surfactant and a basic substance are added and melt-kneaded, and then water is added to cause phase inversion from W / O to O / W. Thus, the aqueous dispersion of the present invention can be obtained.
【0023】なお、(A)及び(B)成分は、単独で溶
融し、上記方法で、水性分散液を得た後、(A)/
(B)=90/10〜10/90の割合で混合しても良い。The components (A) and (B) are melted singly, and an aqueous dispersion is obtained by the above method.
(B) = 90/10 to 10/90 may be mixed.
【0024】非イオン界面活性剤としては、ポリオキシ
エチレンアルキルエステル、ポリオキシエチレンアルキ
ルエーテル、ポリオキシエチレンアルキルフェノールエ
ーテル、ソルビタンアルキルエステル、ポリオキシアル
キレンアルキルエーテル等が例示できる。非イオン界面
活性剤はHLBの異なる2種類を混合して用いても良
い。また、非イオン界面活性剤を主体として少量のアニ
オン性界面活性剤を併用しても良い。Examples of the nonionic surfactant include polyoxyethylene alkyl ester, polyoxyethylene alkyl ether, polyoxyethylene alkyl phenol ether, sorbitan alkyl ester, and polyoxyalkylene alkyl ether. The nonionic surfactant may be used by mixing two kinds having different HLB. Further, a small amount of an anionic surfactant may be used in combination mainly with a nonionic surfactant.
【0025】用いる界面活性剤の量は、(A)カルボン
酸変性塩素化ポリオレフィン及び(B)カルボン酸変性
EVAである樹脂構成成分に対して1〜25重量%が好
ましく、特に3〜15重量%が望ましい。上記界面活性
剤の量が1重量%未満だと水性分散液の安定性が悪くな
り、25重量%を越えると塗膜の付着性、耐水性が悪く
なる。The amount of the surfactant to be used is preferably 1 to 25% by weight, more preferably 3 to 15% by weight, based on the resin components (A) carboxylic acid-modified chlorinated polyolefin and (B) carboxylic acid-modified EVA. Is desirable. If the amount of the surfactant is less than 1% by weight, the stability of the aqueous dispersion will be poor, and if it exceeds 25% by weight, the adhesion and water resistance of the coating film will be poor.
【0026】塩基性物質を加えるのは、カルボキシル基
を中和し、イオン化して水への分散を良好にするためで
あり、塩基性物質を加えないと安定性の良い分散液が得
られない。塩基性物質としては、水酸化ナトリウム、水
酸化カリウム、アンモニア、メチルアミン、エチルアミ
ン、プロピルアミン、ブチルアミン、ヘキシルアミン、
オクチルアミン、エタノールアミン、プロパノールアミ
ン、ジエタノールアミン、N−メチルジエタノールアミ
ン、ジメチルアミン、トリエチルアミン、モルホリン等
を例示できる。The reason why the basic substance is added is to neutralize the carboxyl group and ionize it to improve the dispersion in water. Without adding the basic substance, a stable dispersion cannot be obtained. . As the basic substance, sodium hydroxide, potassium hydroxide, ammonia, methylamine, ethylamine, propylamine, butylamine, hexylamine,
Examples include octylamine, ethanolamine, propanolamine, diethanolamine, N-methyldiethanolamine, dimethylamine, triethylamine, and morpholine.
【0027】用いる塩基性物質の量は、用いる(A)カ
ルボン酸変性塩素化ポリオレフィン及び(B)カルボン
酸変性EVAである樹脂構成成分のカルボキシル基に対
して0.4〜1.5化学当量である事が好ましい。0.
4化学当量未満や1.5化学当量を越える量を用いた場
合には、得られる水性分散液の安定性が悪い。The amount of the basic substance used is 0.4 to 1.5 chemical equivalents based on the carboxyl groups of the resin components (A) the carboxylic acid-modified chlorinated polyolefin and (B) the carboxylic acid-modified EVA. Preferably it is. 0.
If less than 4 chemical equivalents or more than 1.5 chemical equivalents are used, the resulting aqueous dispersion will have poor stability.
【0028】(A)カルボン酸変性塩素化ポリオレフィ
ンが90%を越えた場合、(B)カルボン酸変性EVAの効
果が十分でなく、柔軟性が不足し、かつ特にEVA基材
への付着性が悪い。一方(A)カルボン酸変性塩素化ポ
リオレフィンが10%未満では、特にポリプロピレン系基
材への付着性が低下する。When the content of (A) the carboxylic acid-modified chlorinated polyolefin exceeds 90%, the effect of (B) the carboxylic acid-modified EVA is not sufficient, the flexibility is insufficient, and especially the adhesion to the EVA substrate is poor. bad. On the other hand, if the amount of the carboxylic acid-modified chlorinated polyolefin (A) is less than 10%, the adhesion to a polypropylene-based substrate is particularly reduced.
【0029】このようにして得られた水性分散液は、ポ
リオレフィン系樹脂、特にポリプロピレン及びEVA基
材に対する密着性が優れており、塗膜の柔軟性に優れか
つ粒子径が小さく安定性も良好である。本発明の水性分
散液は、そのままでも顔料を混ぜて使用しても良く、他
の水性樹脂をブレンドしても良い。The aqueous dispersion thus obtained has excellent adhesion to polyolefin-based resins, especially polypropylene and EVA base materials, and has excellent flexibility of the coating film, small particle size and good stability. is there. The aqueous dispersion of the present invention may be used as it is, or may be mixed with a pigment, or may be blended with another aqueous resin.
【0030】本発明の水性分散液は、上塗り塗料の成
分、ポリオレフィンフイルム用のコーティング剤、イン
キ樹脂成分あるいは樹脂成型用、特に自動車内外装材料
であるポリオレフィン系樹脂成型品用のプライマーとし
て使用する事ができる。また素材がEVAである靴の接
着剤用プライマーとしても使用する事ができる。The aqueous dispersion of the present invention may be used as a component of a top coat, a coating agent for a polyolefin film, an ink resin component or a resin molding, particularly as a primer for a polyolefin resin molded article which is an interior / exterior material for automobiles. Can be. It can also be used as an adhesive primer for shoes made of EVA.
【0031】[0031]
【実施例】以下、本発明を実施例により具体的に説明す
るが本発明はこれによって限定されるものではない。EXAMPLES Hereinafter, the present invention will be described specifically with reference to Examples, but the present invention is not limited thereto.
【0032】[製造例1]数平均分子量が30000である
アイソタクチックポリプロピレン500gを、撹拌機と滴下
ロートとモノマーを還流するための冷却管を取り付けた
三口フラスコに入れ、180℃で一定に保たれた油浴中で
完全に溶解した。フラスコ内の窒素置換を約10分間行っ
た後、撹拌を行いながら無水マレイン酸20gを約5分間
かけて投入し、次にジ−t−ブチルパーオキシド2gを
10mlのヘプタンに溶解し、滴下ロートにより約30分間か
けて投入した。この時、系内は180℃に保たれ、さらに
1時間反応を継続した後、アスピレータでフラスコ内を
減圧しながら、約30分間かけて、未反応の無水マレイン
酸を取り除いた。次に、この生成物を反応釜に約300g投
入し、5リットルのクロロホルムを加え、2kg/cm2の圧力下
で十分に溶解した後、紫外線を照射しつつ、塩素含有量
が24重量%になるようにガス状の塩素を反応釜底部より
吹き込んだ。反応終了後、二軸押出機を用いて溶媒であ
るクロロホルムを減圧留去し、カルボキシル基含有塩素
化ポリプロピレンの固形品ペレットを得た。このものの
酸価は26、融点は90℃、数平均分子量は28000であっ
た。[Production Example 1] 500 g of isotactic polypropylene having a number average molecular weight of 30,000 was placed in a three-necked flask equipped with a stirrer, a dropping funnel and a condenser for refluxing monomers, and kept constant at 180 ° C. Dissolved completely in the oil bath. After replacing the nitrogen in the flask for about 10 minutes, 20 g of maleic anhydride was added thereto over about 5 minutes while stirring, and then 2 g of di-t-butyl peroxide was added.
It was dissolved in 10 ml of heptane and charged by a dropping funnel over about 30 minutes. At this time, the inside of the system was kept at 180 ° C., and the reaction was further continued for 1 hour. Then, while reducing the pressure in the flask with an aspirator, unreacted maleic anhydride was removed over about 30 minutes. Next, about 300 g of this product was put into a reaction vessel, and 5 liters of chloroform was added. After sufficiently dissolving under a pressure of 2 kg / cm 2 , while irradiating ultraviolet rays, the chlorine content was reduced to 24% by weight. Gaseous chlorine was blown from the bottom of the reaction vessel so as to make it possible. After completion of the reaction, chloroform as a solvent was distilled off under reduced pressure using a twin-screw extruder to obtain a solid pellet of carboxyl group-containing chlorinated polypropylene. Its acid value was 26, melting point was 90 ° C., and number average molecular weight was 28,000.
【0033】[製造例2]数平均分子量が30000である
エチレン含有量6.1モル%であるエチレン−プロピレン共
重合体500gを、撹拌機と滴下ロートとモノマーを還流す
るための冷却管を取り付けた三口フラスコに入れ、180
℃で一定に保たれた油浴中で完全に溶解した。フラスコ
内の窒素置換を約10分間行った後、撹拌を行いながら無
水マレイン酸33gを製造例1と同様にグラフト共重合さ
せた。次に、この生成物を反応釜に約300g投入し、製造
例1と同様な操作で塩素含有量が18重量%になるように
ガス状の塩素を反応釜底部より吹き込んだ。反応終了
後、二軸押出機を用いて溶媒であるクロロホルムを減圧
留去し、カルボキシル基含有塩素化ポリプロピレンの固
形品ペレットを得た。このものの酸価は62、融点は72
℃、数平均分子量は22000であった。[Production Example 2] 500 g of an ethylene-propylene copolymer having a number average molecular weight of 30,000 and an ethylene content of 6.1 mol% was mixed with a stirrer, a dropping funnel, and a cooling pipe for refluxing the monomer. Place in flask, 180
Dissolved completely in an oil bath kept constant at ° C. After purging with nitrogen in the flask for about 10 minutes, 33 g of maleic anhydride was graft-copolymerized in the same manner as in Production Example 1 while stirring. Next, about 300 g of this product was charged into the reactor, and gaseous chlorine was blown from the bottom of the reactor so as to have a chlorine content of 18% by weight in the same manner as in Production Example 1. After completion of the reaction, chloroform as a solvent was distilled off under reduced pressure using a twin-screw extruder to obtain a solid pellet of carboxyl group-containing chlorinated polypropylene. Its acid value is 62 and melting point is 72
° C, the number average molecular weight was 22,000.
【0034】[製造例3]酢酸ビニル含量28重量%のE
VAをケン化し、ケン化度20のケン化EVAを得た。こ
のケン化EVA100重量部に対し、無水マレイン酸1重
量部、ベンゾイルパーオキサイド0.2重量部をよく混合
し、150℃に設定された押出機で混練押出する事によ
り、メルトフローレートが7.0g/10分で無水マレイン
酸がグラフトされた酸価5のカルボキシル変性EVAを
得た。[Production Example 3] E having a vinyl acetate content of 28% by weight
VA was saponified to obtain saponified EVA having a saponification degree of 20. One part by weight of maleic anhydride and 0.2 part by weight of benzoyl peroxide are mixed well with 100 parts by weight of this saponified EVA, and the mixture is kneaded and extruded with an extruder set at 150 ° C. to give a melt flow rate of 7.0 g / 10. In a minute, a carboxyl-modified EVA having an acid value of 5 to which maleic anhydride was grafted was obtained.
【0035】[製造例4]酢酸ビニル含量28重量%のE
VAをケン化し、ケン化度20のケン化EVAを得た。こ
のケン化EVA100重量部に対し、無水マレイン酸2重
量部、ベンゾイルパーオキサイド0.2重量部をよく混合
し、150℃に設定された押出機で混練押出する事によ
り、メルトフローレートが5.0g/10分で無水マレイン
酸がグラフトされた酸価10のカルボキシル変性EVAを
得た。Production Example 4 E having a vinyl acetate content of 28% by weight
VA was saponified to obtain saponified EVA having a saponification degree of 20. To 100 parts by weight of the saponified EVA, 2 parts by weight of maleic anhydride and 0.2 parts by weight of benzoyl peroxide were thoroughly mixed and kneaded and extruded with an extruder set at 150 ° C. to give a melt flow rate of 5.0 g / 10. In a minute, a carboxyl-modified EVA having an acid value of 10 to which maleic anhydride was grafted was obtained.
【0036】[製造例5]酢酸ビニル含量42重量%のE
VAをケン化し、ケン化度40のケン化EVAを得た。こ
のケン化EVA100重量部に対し、無水マレイン酸3重
量部、ベンゾイルパーオキサイド0.2重量部をよく混合
し、150℃に設定された押出機で混練押出する事によ
り、メルトフローレートが10.0g/10分で無水マレイン
酸がグラフトされた酸価15のカルボキシル変性EVAを
得た。Production Example 5 E having a vinyl acetate content of 42% by weight
VA was saponified to obtain saponified EVA having a saponification degree of 40. To 100 parts by weight of this saponified EVA, 3 parts by weight of maleic anhydride and 0.2 parts by weight of benzoyl peroxide were mixed well, and kneaded and extruded with an extruder set at 150 ° C., so that the melt flow rate was 10.0 g / 10 After that, a carboxyl-modified EVA having an acid value of 15 to which maleic anhydride was grafted was obtained.
【0037】[実施例1]製造例1で得たカルボン酸変
性塩素化ポリオレフィン(A)85g及び製造例3で得た
カルボン酸変性EVA15gを撹拌機付のフラスコに取
り、100℃に加熱溶融させた。その後、非イオン性界面
活性剤10gを加えてよく撹拌し、モルホリン1.5g(0.7化
学当量)を添加した。温度を100℃に保ち、強く撹拌しな
がら、90℃の水を少量ずつ加えた。粘度は上昇したが、
そのまま水を加え続けると粘度は低下した。水を150g加
えたところで内容物を取りだし、乳白色のエマルション
を得た。Example 1 85 g of the carboxylic acid-modified chlorinated polyolefin (A) obtained in Production Example 1 and 15 g of the carboxylic acid-modified EVA obtained in Production Example 3 were placed in a flask equipped with a stirrer, and heated and melted at 100 ° C. Was. Thereafter, 10 g of a nonionic surfactant was added, and the mixture was stirred well, and 1.5 g (0.7 chemical equivalent) of morpholine was added. While maintaining the temperature at 100 ° C., water at 90 ° C. was added little by little with vigorous stirring. Although the viscosity increased,
Continued addition of water reduced the viscosity. When 150 g of water was added, the contents were taken out to obtain a milky white emulsion.
【0038】[実施例2]製造例1で得たカルボン酸変
性塩素化ポリオレフィン(A)70g及び製造例3で得た
カルボン酸変性EVA(B)30gにした以外は、実施例
1と同様な操作を行い、乳白色のエマルションを得た。Example 2 The same procedure as in Example 1 was carried out except that 70 g of the carboxylic acid-modified chlorinated polyolefin (A) obtained in Production Example 1 and 30 g of the carboxylic acid-modified EVA (B) obtained in Production Example 3 were used. The operation was performed to obtain a milky white emulsion.
【0039】[実施例3]製造例1で得たカルボン酸変
性塩素化ポリオレフィン(A)50g及び製造例3で得た
カルボン酸変性EVA(B)50gにした以外は、実施例
1と同様な操作を行い、乳白色のエマルションを得た。Example 3 The same procedure as in Example 1 was performed except that 50 g of the carboxylic acid-modified chlorinated polyolefin (A) obtained in Production Example 1 and 50 g of the carboxylic acid-modified EVA (B) obtained in Production Example 3 were used. The operation was performed to obtain a milky white emulsion.
【0040】[実施例4]製造例1で得たカルボン酸変
性塩素化ポリオレフィン(A)30g及び製造例3で得た
カルボン酸変性EVA(B)70gにした以外は、実施例
1と同様な操作を行い、乳白色のエマルションを得た。Example 4 The same procedure as in Example 1 was carried out except that 30 g of the carboxylic acid-modified chlorinated polyolefin (A) obtained in Production Example 1 and 70 g of the carboxylic acid-modified EVA (B) obtained in Production Example 3 were used. The operation was performed to obtain a milky white emulsion.
【0041】[実施例5]製造例2で得たカルボン酸変
性塩素化ポリオレフィン(A)85g及び製造例3で得た
カルボン酸変性EVA(B)15gにした以外は、実施例
1と同様な操作を行い、乳白色のエマルションを得た。Example 5 The same procedure as in Example 1 was carried out, except that 85 g of the carboxylic acid-modified chlorinated polyolefin (A) obtained in Production Example 2 and 15 g of the carboxylic acid-modified EVA (B) obtained in Production Example 3 were used. The operation was performed to obtain a milky white emulsion.
【0042】[実施例6]製造例2で得たカルボン酸変
性塩素化ポリオレフィン(A)15g及び製造例3で得た
カルボン酸変性EVA(B)85gにした以外は、実施例
1と同様な操作を行い、乳白色のエマルションを得た。Example 6 The same procedure as in Example 1 was carried out except that 15 g of the carboxylic acid-modified chlorinated polyolefin (A) obtained in Production Example 2 and 85 g of the carboxylic acid-modified EVA (B) obtained in Production Example 3 were used. The operation was performed to obtain a milky white emulsion.
【0043】[実施例7]製造例2で得たカルボン酸変
性塩素化ポリオレフィン(A)70g及び製造例4で得た
カルボン酸変性EVA(B)30gにした以外は、実施例
1と同様な操作を行い、乳白色のエマルションを得た。Example 7 The same procedure as in Example 1 was carried out except that 70 g of the carboxylic acid-modified chlorinated polyolefin (A) obtained in Production Example 2 and 30 g of the carboxylic acid-modified EVA (B) obtained in Production Example 4 were used. The operation was performed to obtain a milky white emulsion.
【0044】[実施例8]製造例2で得たカルボン酸変
性塩素化ポリオレフィン(A)70g及び製造例5で得た
カルボン酸変性EVA(B)30gにした以外は、実施例
1と同様な操作を行い、乳白色のエマルションを得た。Example 8 The same procedure as in Example 1 was carried out except that 70 g of the carboxylic acid-modified chlorinated polyolefin (A) obtained in Production Example 2 and 30 g of the carboxylic acid-modified EVA (B) obtained in Production Example 5 were used. The operation was performed to obtain a milky white emulsion.
【0045】[比較例1]製造例1で得たカルボン酸含
有塩素化ポリオレフィン(A)100gを実施例1と同様な
操作を行い、乳白色の水性分散液を得た。Comparative Example 1 The same operation as in Example 1 was carried out on 100 g of the carboxylic acid-containing chlorinated polyolefin (A) obtained in Production Example 1 to obtain a milky white aqueous dispersion.
【0046】[比較例2]製造例3で得たカルボン酸変
性EVA(B)100gを実施例1と同様な操作を行い、乳
白色の水性分散液を得た。Comparative Example 2 The same operation as in Example 1 was carried out on 100 g of the carboxylic acid-modified EVA (B) obtained in Production Example 3 to obtain a milky white aqueous dispersion.
【0047】[実施例9]比較例1,2で得られた水性
分散液を(A)/(B)=70/30で混合して、乳白色の
水性分散液を得た。Example 9 The aqueous dispersions obtained in Comparative Examples 1 and 2 were mixed at (A) / (B) = 70/30 to obtain a milky white aqueous dispersion.
【0048】[実施例10]製造例1で得たカルボン酸
変性塩素化ポリオレフィン(A)及び製造例5で得たカ
ルボン酸変性EVA(B)にした以外は、実施例1と同
様な操作を行い、乳白色のエマルションを得た。Example 10 The same operation as in Example 1 was carried out except that the carboxylic acid-modified chlorinated polyolefin (A) obtained in Production Example 1 and the carboxylic acid-modified EVA (B) obtained in Production Example 5 were used. This gave a milky white emulsion.
【0049】[比較例3]製造例1で得たカルボン酸変
性塩素化ポリオレフィン(A)70g及び市販の無変成E
VA(V5772ET、酸価0、三井デュポンケミカル
(株))30gを実施例1と同様な操作を行った。Comparative Example 3 70 g of the carboxylic acid-modified chlorinated polyolefin (A) obtained in Production Example 1 and commercially available unmodified E
The same operation as in Example 1 was performed using 30 g of VA (V5772ET, acid value 0, Mitsui DuPont Chemical Co., Ltd.).
【0050】[試験例1]各水性分散液の50℃・1ケ月
後における保存安定性結果を表1に示す。比較例3のみ
水性分散液は2層分離したものしか得られなかった。測定方法 ・外観:目視にて判定。 ・pH:25℃の恒温槽に約1時間浸漬した後、pH計に
て測定。 ・平均粒子径:ゼーターサイザー(測定範囲1μm以下、M
ARVARON製)にて測定。Test Example 1 Table 1 shows the results of storage stability of each aqueous dispersion at 50 ° C. for one month. Only in Comparative Example 3, the aqueous dispersion was separated into two layers. Measurement method / Appearance: Determined visually.・ PH: Measured with a pH meter after immersion in a thermostat at 25 ° C for about 1 hour.・ Average particle diameter: Zetasizer (measurement range 1 μm or less, M
ARVARON).
【0051】[試験例2]実施例1〜10の水性分散液
及び比較例1.2の水性分散液をろ過した液をポリプロ
ピレン樹脂板にスプレー塗装し、80℃で30分乾燥した。
次に、二液ウレタン系上塗り塗料を塗装し、10分間室温
で放置し、熱風乾燥器を用いて、80℃で30分間乾燥し
た。得られた塗装板を室温で1日間放置した後、塗膜の
試験を行った。結果を表2に示す。Test Example 2 A solution obtained by filtering the aqueous dispersions of Examples 1 to 10 and the aqueous dispersion of Comparative Example 1.2 was spray-coated on a polypropylene resin plate and dried at 80 ° C. for 30 minutes.
Next, a two-component urethane top coat was applied, left at room temperature for 10 minutes, and dried at 80 ° C. for 30 minutes using a hot air drier. After leaving the obtained coated plate at room temperature for one day, the coating film was tested. Table 2 shows the results.
【0052】試験方法は以下の通りである。 ・付着性 塗膜表面にカッターで素地に達する切れ目を入れて2mm
間隔で100個の碁盤目を作り、その上にセロハン粘着テ
ープを密着させて180度方向に引き剥がし、残存する碁
盤目の数を数えた。剥がれなかった碁盤目数が100なら
○、99以下は×とした。 ・耐ガソリン性 塗膜表面にカッターで素地に達する切れ目を入れて、次
いでレギュラーガソリン中に2時間浸漬した後の塗膜の
切れ目の状態を目視で観察した。塗膜表面に変化が見ら
れない場合には○、フクレ・剥がれ等の外観に変化を生
じた場合には×とした。 ・柔軟性 塗装されたポリプロピレン板を−20℃の冷凍庫に1時間
放置した後、すばやくデュポンの衝撃試験機にセット
し、塗装されたポリプロピレン板を基準として高さ50c
mの位置から500gの硬球を落下させて、塗膜に割れの
生じないものを○、塗膜に割れが生じたものを×とし
た。The test method is as follows.・ Adhesiveness Cut 2m into the surface of the coating film to reach the substrate with a cutter
100 cross-cuts were made at intervals, and a cellophane adhesive tape was stuck thereon and peeled off in the direction of 180 degrees, and the number of remaining cross-cuts was counted. If the number of grids that did not come off was 100, the result was evaluated as ○, and 99 or less was evaluated as ×. -Gasoline resistance A cut was made on the surface of the coating film to reach the substrate with a cutter, and then the state of the cut in the coating film after immersion in regular gasoline for 2 hours was visually observed. When no change was observed on the surface of the coating film, it was evaluated as ○, and when there was a change in appearance such as blistering and peeling, it was evaluated as ×.・ Flexibility After leaving the painted polypropylene plate in a freezer at -20 ° C for 1 hour, quickly set it on a DuPont impact tester, and set the height to 50c based on the painted polypropylene plate.
500 g of hard spheres were dropped from the position of m, and those having no cracks in the coating film were rated as 、, and those having cracks in the coating film were rated as x.
【0053】[試験例3]実施例1〜10の水性分散液
及び比較例1、2の水性分散液をろ過した液をEVA基
材にスプレー塗装し、80℃で30分乾燥した。次に、二液
ウレタン系上塗り塗料を塗装し、10分間室温で放置し、
熱風乾燥器を用いて、80℃で30分間乾燥した。得られた
塗装板を室温で1日間放置した後、塗膜の試験を行っ
た。塗料試験結果を表2に示す。Test Example 3 The aqueous dispersions of Examples 1 to 10 and the aqueous dispersions of Comparative Examples 1 and 2 were filtered and spray-coated on an EVA substrate, and dried at 80 ° C. for 30 minutes. Next, apply a two-component urethane-based topcoat and leave at room temperature for 10 minutes.
It dried at 80 degreeC for 30 minutes using the hot air dryer. After leaving the obtained coated plate at room temperature for one day, the coating film was tested. The coating test results are shown in Table 2.
【0054】試験方法は以下の通りである。 ・付着性 塗膜表面にカッターで素地に達する切れ目を入れて2mm
間隔で100個の碁盤目を作り、その上にセロハン粘着テ
ープを密着させて180度方向に引き剥がし、残存する碁
盤目の数を数えた。剥がれなかった碁盤目数が100なら
○、99以下は×とした。The test method is as follows.・ Adhesiveness Cut 2m into the surface of the coating film to reach the substrate with a cutter
100 cross-cuts were made at intervals, and a cellophane adhesive tape was stuck thereon and peeled off in the direction of 180 degrees, and the number of remaining cross-cuts was counted. If the number of grids that did not come off was 100, the result was evaluated as ○, and 99 or less was evaluated as ×.
【0055】[試験例4]実施例1〜10の水性分散液
及び比較例1、2の水性分散液を靴用基材のEVA発泡
体に乾燥膜厚10μmになるように塗布し、60℃で10分乾
燥した。なお比較として、一般的に使用されている溶剤
系プライマー(エポキシ樹脂系)を塗布した。その後、
水系ウレタン系接着剤100部に対して硬化剤(脂肪族系
ポリイソシアネート)5部を混合したものをEVA基材に100
g/m2になるように塗布した。一方、EVA基材に貼り付け
る塩ビレザーに、EVA基材と同様に水系接着剤及び硬化
剤を100g/m2になるように塗布した。その後、それぞれ6
0℃、10分間乾燥後両者の塗布面同士(EVA基材/塩ビレ
ザー)を貼り合わせた。[Test Example 4] The aqueous dispersions of Examples 1 to 10 and the aqueous dispersions of Comparative Examples 1 and 2 were applied to an EVA foam of a shoe base material so as to have a dry film thickness of 10 μm, and the temperature was 60 ° C. For 10 minutes. For comparison, a commonly used solvent primer (epoxy resin) was applied. afterwards,
A mixture of 100 parts of an aqueous urethane-based adhesive and 5 parts of a curing agent (aliphatic polyisocyanate) is used as an EVA base material.
g / m 2 . On the other hand, an aqueous adhesive and a curing agent were applied to the PVC leather to be adhered to the EVA base material to 100 g / m 2 in the same manner as the EVA base material. Then 6 each
After drying at 0 ° C. for 10 minutes, both coated surfaces (EVA base material / PVC leather) were bonded together.
【0056】その後、試験片を1cm幅になるように切断
し、テンシロンを用いて5kg重、100mm/minの条件でEVA
基材及び塩ビレザーを引き剥がし、その剥離強度を測定
した。3回試験を行い、その平均値を結果とした。結果
を表3に示す。Thereafter, the test piece was cut so as to have a width of 1 cm, and EVA was performed under the conditions of 5 kg weight and 100 mm / min using Tensilon.
The substrate and the PVC leather were peeled off, and the peel strength was measured. The test was performed three times, and the average value was used as the result. Table 3 shows the results.
【0057】[0057]
【表1】表1 保存安定性結果 [Table 1] Table 1 Storage stability results
【0058】測定方法 ・外観:目視にて判定。外観変化無:○ ・pH:25℃の恒温槽に約1時間浸漬した後、pH計に
て測定。 ・平均粒子径:ゼーターサイザー(測定範囲1μm以下、M
ARVARON製)にて測定。 Measurement method / Appearance: Determined visually. No change in appearance: ○-pH: Measured with a pH meter after immersion in a thermostat at 25 ° C for about 1 hour.・ Average particle diameter: Zetasizer (measurement range 1 μm or less, M
ARVARON).
【0059】[0059]
【表2】表2 塗料化試験結果 [Table 2] Table 2 Results of paint test
【0060】[0060]
【表3】表3 引っ張り試験結果 [Table 3] Table 3 Results of tensile test
【0061】表2から、(A)カルボン酸変性塩素化ポ
リオレフィン単独では、柔軟性は得られず、EVA基材
に対して付着性がない。また、(B)カルボン酸変性E
VA単独では、ポリプロピレン基材に対して付着性がな
い。一方、本発明である(A)カルボン酸変性塩素化ポ
リオレフィン及び(B)カルボン酸変性EVAを併用し
た水性分散液は両者に対して有用であることがわかる。
さらに、表3の結果から、本発明である水性分散液は溶
剤系プライマーと同等の引っ張り強度を有する。From Table 2, it can be seen that the carboxylic acid-modified chlorinated polyolefin alone (A) cannot provide flexibility and has no adhesion to the EVA substrate. Further, (B) carboxylic acid-modified E
VA alone has no adhesion to the polypropylene substrate. On the other hand, it can be seen that the aqueous dispersion using (A) the carboxylic acid-modified chlorinated polyolefin and (B) the carboxylic acid-modified EVA in combination is useful for both.
Furthermore, from the results in Table 3, the aqueous dispersion of the present invention has a tensile strength equivalent to that of the solvent-based primer.
【0062】[0062]
【発明の効果】本発明により、ポリオレフィン系樹脂の
成型又はフイルムに対し、塗料、インキ又は接着剤のプ
ライマー用途として優れた付着性、塗膜外観、耐溶剤性
を有し、かつ柔軟性の良好な塗膜を与える水性分散液に
関するものである。すなわち、ポリプロピレン樹脂へは
塗膜の密着性のみならず柔軟性付与効果を与え、かつ靴
等に用いられるEVA系樹脂へも優れた接着力を有する
水性分散液を得る事ができる。Industrial Applicability According to the present invention, it has excellent adhesion, coating appearance, solvent resistance, and good flexibility as a primer for paints, inks, or adhesives for molding or film of a polyolefin resin. The present invention relates to an aqueous dispersion which gives a good coating. That is, it is possible to obtain an aqueous dispersion which gives not only the adhesion of the coating film but also the flexibility to the polypropylene resin, and also has an excellent adhesive force to the EVA resin used for shoes and the like.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C09D 5/00 C09D 5/00 D 5/02 5/02 7/12 7/12 Z 123/26 123/26 123/28 123/28 (72)発明者 小山 欽一郎 山口県岩国市飯田町2−8−1 日本製紙 株式会社化成品開発研究所内 (72)発明者 村本 博則 山口県岩国市飯田町2−8−1 日本製紙 株式会社化成品開発研究所内 Fターム(参考) 4F070 AA12 AA13 AA15 AA16 AB03 AB04 AB09 AC13 AC46 AC84 AE14 CA02 CB02 4J002 BB21W BB21X BB24W CH023 DE056 EH047 EN026 EN106 EU236 FD206 FD313 FD317 GH00 GJ01 HA07 4J038 CB141 CB171 GA06 HA176 HA316 JB03 JB09 KA02 KA09 MA08 MA10 NA01 NA04 NA11 NA12 NA27 PB02 PB07 PC08 4J100 AA02P AA03P AA03Q AA04P AA07P AA15P AA16P AA19P AD02Q AG04Q BA16H BA17H BA18H BB01H BC55H CA01 CA04 CA31 HA08 HA11 HA21 HA57 HB39 HB43 HC29 HC30 HC34 HC43 JA01 JA03 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C09D 5/00 C09D 5/00 D 5/02 5/02 7/12 7/12 Z 123/26 123 / 26 123/28 123/28 (72) Inventor Kinichiro Koyama 2-8-1 Iidacho, Iwakuni City, Yamaguchi Prefecture Nippon Paper Industries Co., Ltd. 8-1 F-term in Nippon Paper Industries Co., Ltd. Chemical Development Laboratory (reference) 4F070 AA12 AA13 AA15 AA16 AB03 AB04 AB09 AC13 AC46 AC84 AE14 CA02 CB02 4J002 BB21W BB21X BB24W CH023 DE056 EH047 EN026 EN106 EU236 FD206 FD313J38 171 GA06 HA176 HA316 JB03 JB09 KA02 KA09 MA08 MA10 NA01 NA04 NA11 NA12 NA27 PB02 PB07 PC08 4J100 AA02P AA03P AA03Q AA04P AA07P AA15P AA16P AA19P AD02Q AG04Q BA16H BA17H BA18H BB0104 BC55H 1 HA08 HA11 HA21 HA57 HB39 HB43 HC29 HC30 HC34 HC43 JA01 JA03
Claims (10)
が(A)塩素含有率が15〜35重量%であるカルボン酸変性
塩素化ポリオレフィンと(B)カルボン酸変性エチレン−
酢酸ビニル共重合体の混合物から成り、塩基性物質、非
イオン界面活性剤を使って水に分散させたことを特徴と
する水性分散液。1. An aqueous dispersion of a resin, wherein the resin components are (A) a carboxylic acid-modified chlorinated polyolefin having a chlorine content of 15 to 35% by weight and (B) a carboxylic acid-modified ethylene-
An aqueous dispersion comprising a mixture of a vinyl acetate copolymer and dispersed in water using a basic substance and a nonionic surfactant.
0〜10/90である請求項1記載の水性分散液。2. The mixing ratio (A) / (B) of the resin component is 90/1.
The aqueous dispersion according to claim 1, wherein the aqueous dispersion is 0 to 10/90.
ンの酸価が10〜100である請求項1又は2記載の水性分
散液。3. The aqueous dispersion according to claim 1, wherein (A) the carboxylic acid-modified chlorinated polyolefin has an acid value of 10 to 100.
ンの数平均分子量が2000〜40000である請求項1〜3い
ずれか1項記載の水性分散液。4. The aqueous dispersion according to claim 1, wherein (A) the carboxylic acid-modified chlorinated polyolefin has a number average molecular weight of 2,000 to 40,000.
ル共重合体の酸価が1〜60である請求項1〜4いずれか
1項記載の水性分散液。5. The aqueous dispersion according to claim 1, wherein (B) the carboxylic acid-modified ethylene-vinyl acetate copolymer has an acid value of 1 to 60.
ル共重合体において、酢酸ビニルがその共重合体の5〜6
0重量%である請求項1〜5いずれか1項記載の水性分
散液。6. The carboxylic acid-modified ethylene-vinyl acetate copolymer (B), wherein vinyl acetate is 5 to 6 of the copolymer.
The aqueous dispersion according to any one of claims 1 to 5, which is 0% by weight.
散液を用いたポリオレフィン基材用の塗料用プライマ
ー。7. A coating primer for a polyolefin substrate, comprising the aqueous dispersion according to claim 1.
散液を用いたポリオレフィン基材用の接着剤用プライマ
ー。8. A primer for an adhesive for a polyolefin substrate, comprising the aqueous dispersion according to claim 1. Description:
酸ビニル共重合体である請求項7記載の塗料用プライマ
ー。9. The primer according to claim 7, wherein the polyolefin substrate is an ethylene-vinyl acetate copolymer.
酢酸ビニル共重合体である請求項8記載の接着剤用プラ
イマー。10. The method according to claim 1, wherein the polyolefin substrate is ethylene-
9. The primer for an adhesive according to claim 8, which is a vinyl acetate copolymer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP34415899A JP3470331B2 (en) | 1999-12-03 | 1999-12-03 | Aqueous dispersion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP34415899A JP3470331B2 (en) | 1999-12-03 | 1999-12-03 | Aqueous dispersion |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2001163984A true JP2001163984A (en) | 2001-06-19 |
| JP3470331B2 JP3470331B2 (en) | 2003-11-25 |
Family
ID=18367090
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP34415899A Expired - Fee Related JP3470331B2 (en) | 1999-12-03 | 1999-12-03 | Aqueous dispersion |
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| Country | Link |
|---|---|
| JP (1) | JP3470331B2 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003106555A1 (en) * | 2002-06-14 | 2003-12-24 | 東洋化成工業株式会社 | Aqueous resin dispersion composition and process for producing the same |
| JP2006225551A (en) * | 2005-02-18 | 2006-08-31 | Unitika Ltd | Aqueous dispersion and laminate |
| JP2010111879A (en) * | 2003-04-18 | 2010-05-20 | Unitika Ltd | Chlorinated polyolefin resin aqueous dispersion |
| US8058354B2 (en) | 2001-02-09 | 2011-11-15 | Eastman Chemical Company | Modified carboxylated polyolefins and their use as adhesion promoters |
| WO2017195828A1 (en) * | 2016-05-13 | 2017-11-16 | 住友化学株式会社 | Aqueous dispersion, coating film, and laminate |
| EP1482010B1 (en) * | 2002-03-05 | 2021-01-13 | Nippon Paper Industries Co., Ltd. | Aqueous dispersion, process for producing the same, and use |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001220474A (en) | 1999-11-30 | 2001-08-14 | Takeda Chem Ind Ltd | Water-based emulsion composition and adhesive composition |
-
1999
- 1999-12-03 JP JP34415899A patent/JP3470331B2/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8058354B2 (en) | 2001-02-09 | 2011-11-15 | Eastman Chemical Company | Modified carboxylated polyolefins and their use as adhesion promoters |
| EP1482010B1 (en) * | 2002-03-05 | 2021-01-13 | Nippon Paper Industries Co., Ltd. | Aqueous dispersion, process for producing the same, and use |
| WO2003106555A1 (en) * | 2002-06-14 | 2003-12-24 | 東洋化成工業株式会社 | Aqueous resin dispersion composition and process for producing the same |
| JP2010111879A (en) * | 2003-04-18 | 2010-05-20 | Unitika Ltd | Chlorinated polyolefin resin aqueous dispersion |
| JP2006225551A (en) * | 2005-02-18 | 2006-08-31 | Unitika Ltd | Aqueous dispersion and laminate |
| WO2017195828A1 (en) * | 2016-05-13 | 2017-11-16 | 住友化学株式会社 | Aqueous dispersion, coating film, and laminate |
| US11149162B2 (en) | 2016-05-13 | 2021-10-19 | Sumitomo Chemical Company, Limited | Aqueous dispersion, coating film, and laminate |
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| Publication number | Publication date |
|---|---|
| JP3470331B2 (en) | 2003-11-25 |
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