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JPH0546849B2 - - Google Patents
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JPH0546849B2 - - Google Patents

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Publication number
JPH0546849B2
JPH0546849B2 JP6904985A JP6904985A JPH0546849B2 JP H0546849 B2 JPH0546849 B2 JP H0546849B2 JP 6904985 A JP6904985 A JP 6904985A JP 6904985 A JP6904985 A JP 6904985A JP H0546849 B2 JPH0546849 B2 JP H0546849B2
Authority
JP
Japan
Prior art keywords
weight
parts
polypropylene resin
carbon black
black
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 - Fee Related
Application number
JP6904985A
Other languages
Japanese (ja)
Other versions
JPS61228029A (en
Inventor
Yoichi Kawai
Masaru Abe
Masami Maki
Yukio Yokote
Katsumi Sekiguchi
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP60069049A priority Critical patent/JPS61228029A/en
Priority to US06/841,265 priority patent/US4734450A/en
Priority to EP86302106A priority patent/EP0200340B1/en
Priority to KR1019860002127A priority patent/KR900002859B1/en
Priority to DE3689861T priority patent/DE3689861T2/en
Priority to CA000504688A priority patent/CA1314644C/en
Priority to CN86102709.4A priority patent/CN1003648B/en
Priority to IN241/CAL/86A priority patent/IN164905B/en
Publication of JPS61228029A publication Critical patent/JPS61228029A/en
Publication of JPH0546849B2 publication Critical patent/JPH0546849B2/ja
Granted legal-status Critical Current

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  • Application Of Or Painting With Fluid Materials (AREA)
  • Coating Of Shaped Articles Made Of Macromolecular Substances (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

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

〔産業上の利用分野〕 本発明は着色されたポリプロピレン系樹脂成形
品の塗装方法に関する。 〔従来の技術〕 従来より、ポリプロピレン樹脂は、そのすぐれ
た化学的、物理的性質、電気的特性のため工業部
品等に広く使用されているが、分子内に極性基を
有しないため、化学的に不活性であり、又、結晶
性が高いため活剤等に対する溶解性が乏しく塗装
性が非常に低い。そのためにポリプロピレン樹脂
の成形品の表面に種々の表面処理を行ない塗装性
を向上させることが行われている。その表面処理
方法としては、火炎処理、コロナ放電処理等があ
るが、成形品形状の制約、表面活性の持続性低
下、塗装の制約等の問題がある。又含ハロゲン系
有機溶剤等による処理方法も行なわれているが、
プライマー工程の必要性、含ハロゲン系有機溶剤
の環境汚染等の問題があり、現在プラズマによる
表面処理後に上塗り塗装を行なう方法が広く行な
われる様になつて来ている。 塗装の対象となるポリプロピレン樹脂成形品
は、全面塗装、部分塗装を問わず無機系、有機系
顔料あるいはこれらの組合わせにより着色されて
いるものが多く、特に屋外等で使用されるものに
ついては、その使用方法を考慮して、耐候性を向
上させることも含めてカーボンブラツク、もしく
は、カーボンブラツクを主体とした黒色系顔料を
添加することが多く、カーボンブラツクの添加量
も多くなつているのが現状である。 しかしながら、この様に、カーボンブラツクを
多量に添加したポリプロピレン樹脂の成形品をプ
ラズマ処理後塗装すると、塗装性が著しく低下す
ることが明らかになつた。 〔発明が解決しようとする問題点〕 本発明の目的は、従来方法の有する種々の欠点
のない着色されたポリプロピレン樹脂の塗装方法
を提供することにある。 〔問題点を解決するための手段〕 本発明者らは、着色されたポリプロピレン系樹
脂成形品の塗装方法を鋭意研究の結果、カーボン
ブラツクの添加量を規定したポリプロピレン系樹
脂成形品をプラズマ処理後に塗装することによ
り、飛躍的に塗装性が向上することを見出し本発
明に至つた。 すなわち本発明は、ポリプロピレン樹脂(A)100
重量部、熱可塑性エラストマー(B)0〜100重量部、
無機フイラー(C)0〜100重量部(但し(B)+(C)/(A)
=1.0以下)から成る樹脂100重量部に対しカーボ
ンブラツクを0.01〜0.6重量部添加したポリプロ
ピレン系樹脂組成物より得られる成形品を、プラ
ズマ処理後塗装することを特徴とするポリプロピ
レン系樹脂組成物の塗装方法である。 本発明に使用されるポリプロピレン樹脂とはプ
ロピレンホモポリマー、エチレン・プロピレン共
重合体、あるいはプロピレンと他のα−オレフイ
ンとの共重合体を意味し、各種ポリエチレンおよ
び他の結晶性樹脂を添加したものでも良い。又必
要に応じて無水マレイン酸等の不飽和カルボン酸
などにより、1部、あるいは全部が変性されたも
のでも差しつかえない。 熱可塑性エラストマーとしては、エチレン・プ
ロピレン共重合体ゴム、エチレン・プロピレン・
ジエン共重合体ゴム、スチレン・ブタジエン共重
合体ゴム、イソブチレン・イソプレン共重合体ゴ
ム等が挙げられる。 無機フイラーは粉末状繊維状の無機フイラーで
あり、例えば酸化カルシウム、酸化マグネシウ
ム、水酸化カルシウム、水酸化マグネシウム、水
酸化アルミニウム、炭酸マグネシウム、ケイ酸カ
ルシウム、ケイ酸マグネシウム、硫酸カルシウ
ム、硫酸マグネシウム、炭酸カルシウム、硫酸バ
リウム、亜硫酸カルシウム、チタン酸カリウム、
タルク、クレー、マイカ、ガラス、塩基性炭酸マ
グネシウム、ドロマイト、等が挙げられる。これ
らの各種無機フイラーは、各種のカツプリング
剤、界面活性剤等で表面処理されたものでも良
く、これらの表面処理は樹脂組成物の剛性、耐衝
撃性の向上に寄与する。 本発明に使用される熱可塑性エラストマーおよ
び無機フイラーの量はポリプロピレン樹脂100重
量部に対し、熱可塑性エラストマーが0〜100重
量部および無機フイラー0〜100重量部であり、
且つ熱可塑性エラストマーと無機フイラーの合計
量が0〜100重量部の範囲であることが望ましく、
熱可塑性エラストマー又は、無機フイラー、及
び、これらの合計量が100重量部を超えて添加さ
れると、得られるポリプロピレン樹脂組成物の剛
性、耐衝撃性等の機械的物性バランス及び塗装性
が低下し好ましくない。 上述のポリプロピレン樹脂に熱可塑性エラスト
マーおよび/または無機フイラーを添加し、また
は添加せずして得られるカーボンブラツク無添加
のポリプロピレン樹脂組成物を以下ベース樹脂と
記す。 本発明において用いられるカーボンブラツクと
しては、一般にポリプロピレン樹脂を黒色に着色
するために使用されるフアーネスブラツク、サー
マルブラツク、チヤンネルブラツク、アセチレン
ブラツク等が挙げられるが、色調、耐熱性、耐候
性等の点で、平均粒子径が5〜40mμのフアーネ
スブラツク、チヤンネルブラツクが好ましく、
又、これらのカーボンブラツクは、2種以上併用
することもできる。カーボンブラツクの平均粒子
径は、上記の範囲のものが好ましく、平均粒子系
が小さいと粒子が二次凝集を起こして分散性が低
下する他、価格も高くなり、又平均粒子径が大き
くなると、色調が悪くなり、耐候性も低下するの
で、いずれの場合も好ましくない。カーボンブラ
ツクの平均粒子径の値は、電子顕微鏡による直接
測定の他、窒素、ヨウ素などの吸着量により求め
た比表面積から球形として産出された値を用い
る。 上記カーボンブラツクの添加量はベース樹脂
100重量部に対し0.01〜0.6重量部、好ましくは
0.05〜0.5重量部であることが必要で、添加量が
0.01重量部未満では耐候性が低下する。その改良
のために一般的に用いられている耐熱、耐候性安
定剤を用いることもできるが特に外装部品の様な
耐候性が必要とされる部品には、これら安定剤を
かなり多量に用いる必要があり、そのため価格が
非常に高くなるほか、成形後に成形品の表面に安
定剤が浮出し、塗装性、外観が低下する等の欠点
があり実用的でない。又、カーボンブラツクの添
加量が0.6重量部を超える場合は、プラズマ処理
後に塗装した塗膜の剥離強度が著しく低下する
他、耐温水試験においてブリスターが起き易くな
り好ましくない。 又、本発明の効果を著しく損なわない程度の範
囲ならば、通常、ポリプロピレン樹脂に添加され
る各種の酸化防止剤、熱安定剤、紫外線吸収剤、
紫外線安定剤:難燃剤、核剤、有機、無機顔料等
を単独、あるいは併用しても差しつかえない。 本発明におけるポリプロピレン系樹脂組成物
は、当業界で一般に用いられるヘンシエルミキサ
ー等を用いて混合を行なつた後、単軸押出機、
FCM、CIM等の2軸押出機、ロール、バンバリ
ーミキサー等を用いて混練を行ない、ペレツト化
されることが多い。 本発明に使用される成形品は、上記の方法によ
り得られた樹脂組成物を通常用いられる射出成形
法、押出成形法、または圧縮成形法等の成形法に
より得られる。 プラズマによる成形品の表面処理方法として
は、通常、高周波、マイクロ波放電等により、酸
素、窒素、あるいは他の不活性ガス等及びこれら
の混合ガスを励起させたプラズマを成形品の表面
に接触させて行なうことができる。その処理条件
としては、ガスの種類により多少異なるが通常圧
力としては0.1〜5Torrで、処理時間は、5〜600
秒程度である。成形品の形状によつては処理時間
を長くしたり、処理槽の形状に変化を設ける必要
性も生じる。 以下実施例によつて本発明を具体的に説明す
る。 〔実施例〕 実施例 1〜5 メルトフローインデツクス4.0であるポリプロ
ピレンホモポリマー(PP−A)100重量部に対し
2,6−ジ−tert−ブチル−4−メチルフエノー
ル0.05重量部、ステアリン酸カルシウム0.1重量
部、テトラキス〔メチレン−3−(3′,5′−ジ−
tert−ブチル−4′−ヒドロキシフエニル)プロピ
オネート〕メタン0.2重量部、ビス(2,2,6,
6−テトラメチル−4−ピペリジル)セバケート
0.4重量部、2−(3−tert−ブチル−5−メチル
−2−ヒドロキシフエニル)−5−クロロベンゾ
トリアゾール0.2重量部および、平均粒子径が24
mμのフアーネスブラツク(カーボンブラツク
A)、平均粒子径が18mμであるチヤンネルブラ
ツク(カーボンブラツクB)を表−1に示す量配
合し、ヘンシエルミキサーで混合後、温度を230
℃に設定した40mmφ押出機にてペレツト化し、得
られた樹脂組成物を射出成形にてテストピース
(80×160×2mm平板)を得た。 このテストピースを下記の条件にてプラズマ処
理を行なつた後、2液型ウレタン系の上塗り用塗
料を膜厚50μmとなるように塗装し、90℃で40分
間乾燥した後、室温で48時間放置して、塗装品を
得た。この塗装品の塗膜に、カツターにより巾
1.0cmの切り込みを入れインストロン引張試験機
にて塗膜の180゜剥離強度を測定した。 また、この塗装品を40℃の温水中に浸し240時
間後の塗膜の状態を目視により判定した。 ●プラズマ処理条件 (1) プラズマ処理装置 東芝製マイクロ波プラ
ズマ処理装置(TMZ−2026M) (2) 処理ガス 酸素 (3) 処理時間 30秒 (4) ガス圧力 1.0Torr (5) ガス流量 480c.c./min (6) マイクロ波出力 1500W ●塗膜の状態の判定基準 ○:塗膜のブリスター 全くなし △:塗膜のブリスター ややあり ×:塗膜のブリスター かなりあり 結果を表−1に示す。 実施例 6 実施例1のPP−Aにかえて、エチレン含量8
重量%、メルトフローインデツクス3.8/10min
のエチレン・ブロピレンブロツク共重合体(PP
−B)を用い、カーボンブラツクAの添加量を表
−1に示す値とした他は実施例1と同様に試験
し、得られた結果を表−1に示す。 実施例 7、8 実施例6においてPP−B100重量部に対しプロ
ピレン含量26%、100℃でのムーニー粘度が24で
あるエチレン・プロピレン共重合体ゴム(EPR
−A)を20重量部、40重量部添加した他は、実施
例6と同様に試験し得られた結果を表−1に示
す。 実施例 9、10 実施例6において、PP−B100重量部に対し、
平均粒子径3.2μmであるタルクを10重量部、20重
量部添加した他は実施例6と同様に試験し、得ら
れた結果を表−1に示す。 実施例 11 実施例6においてPP−B100重量部に対し平均
粒子径2.5μmの炭酸カルシウムを20重量部添加し
た他は実施例6と同様に試験し、得られた結果を
表−1に示す。 実施例 12〜14 PP−B、EPR−A、タルク、炭酸カルシウム
の配合量を表−1に示す割合とし、実施例6と同
様に試験した。得られた結果を表−1に示す。 比較例 1〜5 実施例:1、4、6、7、12において、カーボ
ンブラツク−A又は−Bの添加量を各々のベース
樹脂、100重量部に対し表−1に示す割合とした
他は実施例1と同様に試験し得られた結果を表−
1に示す。
[Industrial Field of Application] The present invention relates to a method for coating colored polypropylene resin molded articles. [Prior Art] Polypropylene resin has traditionally been widely used in industrial parts due to its excellent chemical, physical, and electrical properties. Also, because it is highly crystalline, it has poor solubility in active agents and has very low paintability. To this end, various surface treatments have been carried out on the surface of polypropylene resin molded articles to improve paintability. The surface treatment methods include flame treatment, corona discharge treatment, etc., but there are problems such as restrictions on the shape of the molded product, reduced sustainability of surface activity, and restrictions on painting. Treatment methods using halogen-containing organic solvents are also used, but
Due to problems such as the necessity of a priming process and environmental pollution caused by halogen-containing organic solvents, a method of applying a topcoat after surface treatment with plasma has become widely used. Many polypropylene resin molded products that are subject to painting are colored with inorganic or organic pigments, or a combination of these, regardless of whether they are fully or partially painted.Particularly for those used outdoors, etc. Considering the method of use, carbon black or a black pigment mainly composed of carbon black is often added to improve weather resistance, and the amount of carbon black added is also increasing. This is the current situation. However, it has become clear that when a polypropylene resin molded article to which a large amount of carbon black has been added is painted after plasma treatment, the paintability is significantly reduced. [Problems to be Solved by the Invention] An object of the present invention is to provide a method for coating colored polypropylene resins that does not have the various drawbacks of conventional methods. [Means for Solving the Problems] As a result of intensive research on the method of coating colored polypropylene resin molded products, the present inventors found that after plasma treatment, polypropylene resin molded products with a specified amount of carbon black added The present inventors have discovered that painting improves the paintability dramatically. That is, the present invention uses polypropylene resin (A) 100
parts by weight, thermoplastic elastomer (B) 0 to 100 parts by weight,
Inorganic filler (C) 0 to 100 parts by weight ((B) + (C) / (A)
A polypropylene resin composition obtained by adding 0.01 to 0.6 parts by weight of carbon black to 100 parts by weight of a resin consisting of 1.0 or less) is coated after plasma treatment. This is a painting method. The polypropylene resin used in the present invention means a propylene homopolymer, an ethylene/propylene copolymer, or a copolymer of propylene and other α-olefins, to which various polyethylenes and other crystalline resins are added. But it's okay. Further, if necessary, it may be partially or entirely modified with an unsaturated carboxylic acid such as maleic anhydride. Thermoplastic elastomers include ethylene/propylene copolymer rubber, ethylene/propylene copolymer rubber,
Examples include diene copolymer rubber, styrene/butadiene copolymer rubber, isobutylene/isoprene copolymer rubber, and the like. The inorganic filler is a powdered fibrous inorganic filler, such as calcium oxide, magnesium oxide, calcium hydroxide, magnesium hydroxide, aluminum hydroxide, magnesium carbonate, calcium silicate, magnesium silicate, calcium sulfate, magnesium sulfate, carbonate. Calcium, barium sulfate, calcium sulfite, potassium titanate,
Examples include talc, clay, mica, glass, basic magnesium carbonate, dolomite, and the like. These various inorganic fillers may be surface-treated with various coupling agents, surfactants, etc., and these surface treatments contribute to improving the rigidity and impact resistance of the resin composition. The amounts of the thermoplastic elastomer and inorganic filler used in the present invention are 0 to 100 parts by weight of the thermoplastic elastomer and 0 to 100 parts by weight of the inorganic filler, based on 100 parts by weight of the polypropylene resin.
Further, it is desirable that the total amount of the thermoplastic elastomer and the inorganic filler is in the range of 0 to 100 parts by weight,
If the thermoplastic elastomer or inorganic filler or the total amount thereof exceeds 100 parts by weight, the balance of mechanical properties such as rigidity and impact resistance and paintability of the resulting polypropylene resin composition will deteriorate. Undesirable. A carbon black-free polypropylene resin composition obtained by adding or not adding a thermoplastic elastomer and/or an inorganic filler to the above-mentioned polypropylene resin is hereinafter referred to as a base resin. Examples of the carbon black used in the present invention include furnace black, thermal black, channel black, acetylene black, etc., which are generally used to color polypropylene resin black. In this respect, furnace black and channel black with an average particle diameter of 5 to 40 mμ are preferable.
Moreover, two or more types of these carbon blacks can also be used in combination. The average particle size of carbon black is preferably within the above range; if the average particle size is small, the particles will cause secondary aggregation and the dispersibility will decrease, and the price will also increase; Either case is unfavorable since the color tone becomes poor and the weather resistance also decreases. The value of the average particle diameter of carbon black is determined not only by direct measurement using an electron microscope, but also by the value obtained as a sphere based on the specific surface area determined from the adsorption amount of nitrogen, iodine, etc. The amount of carbon black added above is based on the base resin.
0.01 to 0.6 parts by weight per 100 parts by weight, preferably
It is necessary that the amount is 0.05 to 0.5 parts by weight, and the amount added is
If it is less than 0.01 part by weight, weather resistance will decrease. To improve this, commonly used heat-resistant and weather-resistant stabilizers can be used, but especially for parts that require weather resistance, such as exterior parts, it is necessary to use quite a large amount of these stabilizers. This makes it extremely expensive, and it is not practical because the stabilizer stands out on the surface of the molded product after molding, reducing paintability and appearance. Furthermore, if the amount of carbon black added exceeds 0.6 parts by weight, the peel strength of the coating film applied after plasma treatment will be markedly reduced, and blistering will easily occur in the hot water resistance test, which is not preferable. In addition, various antioxidants, heat stabilizers, ultraviolet absorbers,
Ultraviolet stabilizer: Flame retardant, nucleating agent, organic or inorganic pigment, etc. may be used alone or in combination. The polypropylene resin composition of the present invention is mixed using a Henschel mixer or the like commonly used in the industry, and then mixed using a single-screw extruder.
It is often kneaded and pelletized using a twin-screw extruder such as FCM or CIM, rolls, or a Banbury mixer. The molded article used in the present invention is obtained by a commonly used molding method such as an injection molding method, an extrusion molding method, or a compression molding method using the resin composition obtained by the above method. The surface treatment method for molded products using plasma usually involves bringing plasma excited by oxygen, nitrogen, other inert gases, or a mixture of these gases into contact with the surface of the molded product using high frequency, microwave discharge, etc. can be done. The processing conditions vary slightly depending on the type of gas, but the normal pressure is 0.1 to 5 Torr, and the processing time is 5 to 600 Torr.
It is about seconds. Depending on the shape of the molded product, it may be necessary to lengthen the treatment time or change the shape of the treatment tank. The present invention will be specifically explained below using Examples. [Example] Examples 1 to 5 0.05 part by weight of 2,6-di-tert-butyl-4-methylphenol and 0.1 part by weight of calcium stearate per 100 parts by weight of polypropylene homopolymer (PP-A) having a melt flow index of 4.0. Parts by weight, tetrakis [methylene-3-(3',5'-di-
tert-butyl-4'-hydroxyphenyl)propionate] 0.2 parts by weight of methane, bis(2,2,6,
6-tetramethyl-4-piperidyl) sebacate
0.4 parts by weight, 0.2 parts by weight of 2-(3-tert-butyl-5-methyl-2-hydroxyphenyl)-5-chlorobenzotriazole, and an average particle size of 24
A furnace black (carbon black A) with an average particle diameter of 18 mμ and a channel black (carbon black B) with an average particle diameter of 18 mμ were mixed in the amounts shown in Table 1, and after mixing with a Henschel mixer, the temperature was set to 230 °C.
The resin composition was pelletized using a 40 mmφ extruder set at ℃, and the resulting resin composition was injection molded to obtain a test piece (80 x 160 x 2 mm flat plate). This test piece was subjected to plasma treatment under the following conditions, then coated with a two-component urethane topcoat to a film thickness of 50 μm, dried at 90°C for 40 minutes, and then kept at room temperature for 48 hours. I left it alone and got a painted product. The width of the cutter is applied to the coating film of this painted product.
A 1.0 cm cut was made and the 180° peel strength of the coating film was measured using an Instron tensile tester. In addition, the coated product was immersed in warm water at 40°C and the state of the coating film was visually determined after 240 hours. ●Plasma processing conditions (1) Plasma processing equipment Toshiba microwave plasma processing equipment (TMZ-2026M) (2) Processing gas Oxygen (3) Processing time 30 seconds (4) Gas pressure 1.0Torr (5) Gas flow rate 480c.c ./min (6) Microwave output 1500W ●Judgment criteria for paint film condition ○: No blisters in the paint film △: Some blisters in the paint film ×: Quite a few blisters in the paint film The results are shown in Table-1. Example 6 Instead of PP-A in Example 1, ethylene content was 8
Weight%, melt flow index 3.8/10min
Ethylene-propylene block copolymer (PP)
-B) was used, and the test was conducted in the same manner as in Example 1, except that the amount of carbon black A added was set to the value shown in Table 1, and the obtained results are shown in Table 1. Examples 7 and 8 In Example 6, ethylene-propylene copolymer rubber (EPR) with a propylene content of 26% and a Mooney viscosity of 24 at 100°C was used with respect to 100 parts by weight of PP-B.
Table 1 shows the results obtained by testing in the same manner as in Example 6, except that 20 parts by weight and 40 parts by weight of -A) were added. Examples 9 and 10 In Example 6, for 100 parts by weight of PP-B,
The test was carried out in the same manner as in Example 6, except that 10 parts by weight and 20 parts by weight of talc having an average particle diameter of 3.2 μm were added, and the results obtained are shown in Table 1. Example 11 Tests were carried out in the same manner as in Example 6, except that 20 parts by weight of calcium carbonate having an average particle size of 2.5 μm were added to 100 parts by weight of PP-B, and the results are shown in Table 1. Examples 12 to 14 Tests were conducted in the same manner as in Example 6, using the proportions of PP-B, EPR-A, talc, and calcium carbonate shown in Table 1. The results obtained are shown in Table-1. Comparative Examples 1 to 5 In Examples 1, 4, 6, 7, and 12, the addition amount of carbon black-A or -B was changed to the ratio shown in Table 1 to 100 parts by weight of each base resin. The results obtained by testing in the same manner as in Example 1 are shown in the table below.
Shown in 1.

【表】【table】

【表】【table】

【表】【table】

〔発明の効果〕〔Effect of the invention〕

本発明の方法により、従来種々問題のあつた着
色されたポリプロピレン系樹脂組成物の成形品に
対し、塗膜の剥離強度、耐湿性等のきわめてすぐ
れた塗装が可能となつた。
By the method of the present invention, it has become possible to coat molded articles of colored polypropylene resin compositions, which have conventionally had various problems, with extremely excellent peel strength and moisture resistance.

Claims (1)

【特許請求の範囲】 1 ポリプロピレン樹脂(A)100重量部、熱可塑性
エラストマー(B)0〜100重量部、無機フイラー(C)
0〜100重量部(但し(B)+(C)/(A)=1.0以下)から成 る樹脂100重量部に対し、カーボンブラツクを
0.01〜0.6重量部添加したポリプロピレン系樹脂
組成物より得られる成形品をプラズマ処理後塗装
することを特徴とするポリプロピレン系樹脂成形
品の塗装方法。
[Claims] 1. 100 parts by weight of polypropylene resin (A), 0 to 100 parts by weight of thermoplastic elastomer (B), inorganic filler (C)
Add carbon black to 100 parts by weight of resin consisting of 0 to 100 parts by weight (however, (B) + (C) / (A) = 1.0 or less).
A method for coating a polypropylene resin molded article, which comprises coating a molded article obtained from a polypropylene resin composition containing 0.01 to 0.6 parts by weight after plasma treatment.
JP60069049A 1985-03-22 1985-04-03 Painting of polypropylene resin molded article Granted JPS61228029A (en)

Priority Applications (8)

Application Number Priority Date Filing Date Title
JP60069049A JPS61228029A (en) 1985-04-03 1985-04-03 Painting of polypropylene resin molded article
US06/841,265 US4734450A (en) 1985-03-22 1986-03-19 Polypropylene-base resin composition containing an inorganic filler and 0.01 to 0.6 wt. % of carbon black
EP86302106A EP0200340B1 (en) 1985-03-22 1986-03-21 Polypropylene-base resin composition
KR1019860002127A KR900002859B1 (en) 1985-03-22 1986-03-21 Resin composition based on polypropylene
DE3689861T DE3689861T2 (en) 1985-03-22 1986-03-21 Polypropylene compositions.
CA000504688A CA1314644C (en) 1985-03-22 1986-03-21 Polypropylene-base resin composition
CN86102709.4A CN1003648B (en) 1985-03-22 1986-03-22 Formulation of Polypropylene Matrix Resin
IN241/CAL/86A IN164905B (en) 1985-03-22 1986-03-24

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60069049A JPS61228029A (en) 1985-04-03 1985-04-03 Painting of polypropylene resin molded article

Publications (2)

Publication Number Publication Date
JPS61228029A JPS61228029A (en) 1986-10-11
JPH0546849B2 true JPH0546849B2 (en) 1993-07-15

Family

ID=13391328

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60069049A Granted JPS61228029A (en) 1985-03-22 1985-04-03 Painting of polypropylene resin molded article

Country Status (1)

Country Link
JP (1) JPS61228029A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01118557A (en) * 1987-10-30 1989-05-11 Mitsubishi Motors Corp Resin composition
DE102007054242A1 (en) * 2007-11-14 2009-05-20 Basf Coatings Ag Method for setting defined morphologies of segregated phases in thin layers

Also Published As

Publication number Publication date
JPS61228029A (en) 1986-10-11

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