JP4076395B2 - Polypropylene paint molding - Google Patents

Description

なお、これらのペンタッドに由来するピークのケミカルシフトは、ＮＭＲの測定条件によって多少の変動があること、および、ピークは必ずしも単一ピーク（single peak）ではなく、微細構造にもとづく複雑な分裂パターン（split pattern）を示すことが多い点に注意して帰属を行う必要がある。本発明でいうアイソタクチックブロックとは、ｍｍｍｍペンタッドを指称し、非晶性ブロックとは、少なくとも１個のｒダイアドを含む他の全てのペンタッドを指称する。
【００２７】
本発明において、ステレオブロック構造の特徴として重要なところは、下記要件＜１＞及び＜２＞である。
＜１＞ ｍｍｍｍで表されるペンタッドに帰属されるピークのピークトップのケミカルシフトを２１．８ｐｐｍとした際に、１９．８〜２２．２ｐｐｍの範囲に現れる上記１０種類のペンタッドに属するピークの総面積Ｓに対する、２１．８ｐｐｍをピークトップとするピークの面積Ｓ₁の比率（Ｓ₁／Ｓ）が２０〜６０％であること
＜２＞ ２１．５〜２１．７ｐｐｍにピークトップを有するピーク（ｍｍｍｒ）の面積をＳ₂としたとき、Ｓ₁とＳ₂の関係が、４＋２Ｓ₁／Ｓ₂＞５を満たすこと。
【００２８】
Ｓに対するＳ₁の比率が１０％未満である場合には、結晶性が低すぎ、十分な塗膜密着性が得られず、さらに、べたつきなどの問題も起こりやすいために好ましくない。一方、Ｓに対するＳ₁の比率が６０％を越える場合には、逆に結晶性が高すぎ、溶媒への溶解性が低下するため、これも好ましくない。Ｓに対するＳ₁の比率は、好ましくは２０〜５０％、更に好ましくは３０〜５０％である。
【００２９】
Ｓ₁とＳ₂を上記の要件＜２＞で規定した範囲となるように制御する方法としては、（ｉ）重合触媒の構造によって制御する方法、（ｉｉ）重合温度によって制御する方法、（ｉｉｉ）モノマー濃度によって制御する方法；等を挙げることができる。Ｓ₁、Ｓ₂の温度依存性や、モノマー濃度依存性は、使用する触媒によって異なるので一概に言うことはできない。したがって、使用する触媒の性質にもとづいて、これらの条件を制御することが肝要である。また、重合触媒の構造によって制御する場合には、遷移金属成分を構成する配位子の構造が重要である。特に、架橋メタロセンを用いる場合には、架橋基の橋頭を基点として α−位の置換基が重要である。一般的には、α−位にある程度かさだかい置換基がある場合に、立体選択性が向上しやすい。さらに、インデニル基やアズレニル基などの縮合環を有する配位子を含む架橋メタロセンを用いる場合には、４−位の置換基の構造も立体選択性に大きな影響を与える。一般的には、４−位にある程度かさだかい置換基がある場合に、立体選択性が向上しやすい。逆に、４−位に、立体的に比較的小さい置換基を導入することにより、効果的に立体選択性を低下させ、生成重合体の結晶性を低下させるという制御が可能となる。
【００３０】
更に本発明のステレオブロック構造の特徴として、下記要件＜３＞〜＜１０＞が挙げられる。これらの要件は、いずれも、プロピレン系重合体主鎖中に結晶性の高いブロックと非晶性の高いブロックが共存し、かつ、結晶性の高いブロックがアイソタクチック性に富む構造となっていることと密接に関係している。
＜３＞ ２０．３〜２０．５ｐｐｍにピークトップを有するピーク（ｒｒｒｒ）の面積をＳ₃とした際、その面積Ｓ₃の比率（Ｓ₃／Ｓ）が０．２〜３％であること
＜４＞ ２０．６〜２０．８ｐｐｍにピークトップを有するピーク（ｒｍｒｍ）の面積をＳ₄とした際、その面積Ｓ₄の比率（Ｓ₄／Ｓ）が０．３〜７％であること
＜５＞ Ｓ₄がＳ₃よりも大きいこと、
＜６＞ Ｓ₁とＳ₂の関係が、２５＞４＋２Ｓ₁／Ｓ₂＞５を満たすこと
＜７＞ 面積Ｓ₁の比率（Ｓ₁／Ｓ）が３０〜５０％であること
＜８＞ 面積Ｓ₃の比率（Ｓ₃／Ｓ）が１〜３％であること
＜９＞ 面積Ｓ₄の比率（Ｓ₄／Ｓ）が４〜７％であること、
＜１０＞Ｓ₁とＳ₂の関係が、１０＞４＋２Ｓ₁／Ｓ₂＞７を満たすこと
【００３１】
プロピレン系重合体主鎖は、要件＜２＞の如く、４＋２Ｓ₁／Ｓ₂＞５という関係を満足することが好ましい。この関係式は、Ｗａｙｍｏｕｔｈらによりアイソタクチックブロックインデックス（ＢＩ）と名づけられた指数（特表平９−５１０７４５号公報参照）と密接な関連がある。ＢＩは、重合体のステレオブロック性を表す指標であり、ＢＩ＝４＋２［ｍｍｍｍ］／［ｍｍｍｒ］で定義される。より具体的には、ＢＩは、４個以上のプロピレン単位を有するアイソタクチックブロックの平均連鎖長を表す（Ｊ．Ｗ．Ｃｏｌｌｅｔｅ ｅｔａｌ．，Ｍａｃｒｏｍｏｌ．，２２，３８５８（１９８９）；Ｊ．Ｃ．Ｒａｎｄａｌｌ，Ｊ．Ｐｏｌｙｍ．Ｓｃｉ．Ｐｏｌｙｍ．Ｐｈｙｓ．Ｅｄ．，１４，２０８３（１９７６））。統計的に完全なアタクチックポリプロピレンの場合、ＢＩ＝５となる。したがって、ＢＩ＝４＋２［ｍｍｍｍ］／［ｍｍｍｒ］＞５とは、重合体中に含まれるアイソタクチックブロックの平均連鎖長が、アタクチックポリプロピレンのそれよりも長いことを意味する。
【００３２】
要件＜２＞、＜６＞又は＜１０＞における、４＋２Ｓ₁／Ｓ₂は、上述のＢＩと完全には同一でないものの、おおむね対応していることから、４＋２Ｓ₁／Ｓ₂＞５という要件＜２＞は、本発明の重合体主鎖が、アタクチックポリプロピレンとは異なり、結晶化可能な連鎖長のアイソタクチックブロックを含有することを意味する。また、アタクチックブロックが存在するということは、言い換えれば、立体特異性（ｓｔｅｒｅｏｓｐｅｃｉｆｉｃｉｔｙ）が乱れたシークエンスからなるブロックも同時に主鎖に存在することを意味する。このように、主鎖中に結晶性を有するブロックと非晶性のブロックとが共存し、かつ、結晶性を有するブロックが、比較的長い平均連鎖長を有するアイソタクチックブロックから形成され、アイソタクチック性に富む構造になっているという特異な構造である。
【００３３】
特性（４） ２５℃におけるトルエンに１０重量％の濃度で溶解した際に、その不溶分が１重量％以下であること
室温のトルエン（２５℃）に１０重量％濃度で溶解した場合、特性（２）と同様レベルの溶解性を示すものが好ましい。
測定方法としては、例えば次のように所定温度・所定濃度で溶解した溶液をその温度付近にて（温度が高い場合によっては熱時濾過）濾過し、その時用いた濾紙もしくはＳＵＳ製金網（あらかじめ重量を測ってある）を乾燥し、不溶分の重量を測定する方法が用いられる。
トルエン不溶分が１重量％を超えると、溶解性が不足するために、塗膜の肌荒れや平滑性などの塗装性能が低下する傾向があり、さらに塗料として用いた場合の溶液状態の貯蔵安定性が悪化し分離しやすくなる傾向があり塗装工程における作業性が低下するため好ましくない。
【００３４】
特性（５） ＧＰＣで測定した重量平均分子量Ｍｗが５，０００〜１００万である
ＧＰＣ（Gel Permeation Chromatography）で測定した重量平均分子量Ｍｗが５，０００〜１００万であることが好ましい。Ｍｗが５，０００より小さい場合には、グラフト共重合により変性した極性基含有プロピレン系重合体を用いて基材上に塗布した後の造膜性が悪化するばかりでなく、べたつきもあり好ましくない。また、Ｍｗが１００万を越える場合には、造膜性やべたつきについては大きな問題はないものの、極性基含有プロピレン系重合体を溶媒に溶解した際の粘度が高くなりすぎ、製造上あるいは該極性基含有プロピレン系重合体溶液のハンドリング上、不都合を生じるために好ましくない。本発明において、好ましい重量平均分子量Ｍｗの範囲は５，０００〜１００万であるが、より好ましくは、１０，０００〜５０万、さらに好ましくは、３０，０００〜２０万である。
【００３５】
重合体の分子量調節には、従来公知の方法を使用することができる。すなわち、重合温度を制御して分子量を調節する方法、モノマー濃度を制御して分子量を調節する方法、連鎖移動剤を使用して分子量を制御する方法が挙げられる。連鎖移動剤を使用する場合には、水素が好ましい。
なお、ＧＰＣによる分子量の測定は、オルトジクロロベンゼンを溶媒とし、ポリスチレンを標準試料として、市販の装置を用いて従来公知の方法で行うことができる。
分子量分布については、特に制限はないが、過度に広すぎる分子量分布は、低分子量成分の含有量が必然的に多いことを意味するので避けた方が良い。分子量分布の指標として重量平均分子量Ｍｗと数平均分子量Ｍｎとの比Ｍｗ／Ｍｎを用いた場合、好ましくはＭｗ／Ｍｎ＜２０、さらに好ましくはＭｗ／Ｍｎ＜１０、最も好ましくはＭｗ／Ｍｎ＜５のものが好適に使用される。
【００３６】
特性（６） ＤＳＣで測定した結晶融解熱量が１Ｊ／ｇ以上に相当する明確なピークが存在しないこと
プロピレン系重合体主鎖においては、結晶融解熱が１Ｊ／ｇに相当する明確なピークが存在すると、溶媒への溶解性が低下するので好ましくない。測定方法としては、熱分析システム（ＤＳＣ）を用いて、試料を２００℃で３分間融解後、１０℃／分の速度で３０℃まで降温し、１０℃／分で２００℃まで昇温することにより融解曲線を得る。最後の昇温段階における融解曲線から、５０〜１６０℃の温度域において、１Ｊ／ｇ以上に相当する明確なピークが存在するか否かを評価する。ピークが存在する場合、ピークトップ温度を融点とし、吸熱ピーク面積から結晶融解熱を求めた。
【００３７】
特性（７） ６０℃のオルトジクロロベンゼン（ＯＤＣ）に実質的に全て溶解すること
プロピレン系重合体主鎖は、特性（３）で述べたように、メチル基の立体規則性分布が適度であるので、その結晶性も比較的低く溶媒に対する溶解性に優れる特徴を有する。具体的には、重合体をオルトジクロロベンゼン（ＯＤＣ）にて昇温溶出分別した際に、実質的にすべての成分が６０℃以下で溶出するという特性である。６０℃よりも高い温度で溶出する成分は、結晶性がかなり高い成分であるので、重合体がこのような成分を含んでいる場合には、重合体を溶媒に溶解させた際に、こうした結晶性の高い成分が不溶成分となったり、ゲル化が発生したりするといった不都合が起きやすい。好ましくは５０℃以下、さらに好ましくは４０℃以下で実質的にすべての成分が溶出することが好ましい。
【００３８】
プロピレン系重合体主鎖は、特性（２）（４）（７）で述べたように有機溶媒に対する溶解性に優れる。ヘプタン、トルエン、オルトジクロロベンゼン以外の有機溶媒としては、ベンゼン、キシレン等の芳香族系炭化水素；ｎ−ペンタン、ｎ−ヘキサン、ｎ−オクタン、ｎ−デカン等の脂肪族系炭化水素；シクロヘキサン、メチルシクロヘキサン、ジメチルシクロヘキサン等の脂環式脂肪族系炭化水素、塩化メチレン、四塩化炭素、トリクロロエチレン、パークロルエチレン、クロルベンゼン等のハロゲン化炭化水素、ｎ−エチルアセテート、ｎ−ブチルアセテート等のエステル類、メチルイソブチルケトン、シクロヘキサノン等のケトン類、テトラヒドロフラン、ジメチルスルホキシド等の極性溶媒類などが挙げられる。これらの中でも、芳香族炭化水素もしくはハロゲン化炭化水素が好ましく、特にトルエン、キシレン、クロルベンゼンが好ましい。
これらの有機溶媒は、プロピレン系重合体主鎖の変性反応の溶媒あるいは変性反応物を溶解する塗料ビヒクルとして好適に用いられる。
【００３９】
次に、極性基含有プロピレン系重合体の極性基について説明する。本発明において、「極性基」とは、カルボキシル基、カルボン酸無水物基又はカルボン酸エステル基の総称であり、極性基含有プロピレン系重合体の側鎖に相当するものである。
プロピレン系重合体主鎖に極性基を導入する方法として、カルボキシル基等を含有する重合性単量体をグラフト共重合させる方法が一般的である。
【００４０】
グラフト共重合させるカルボキシル基を含有する重合性単量体としては、（メタ）アクリル酸およびその酸誘導体並びにモノオレフィンジカルボン酸、その無水物およびそのモノエステル類が挙げられ、これらから選ばれる少なくとも１種が用いられる。具体的に例示するならば、（メタ）アクリル酸およびそのエステル誘導体としては（メタ）アクリル酸；炭素数１〜１２のアルキル基を有する（メタ）アクリル酸エステル系モノマー、例えば（メタ）アクリル酸メチル、（メタ）アクリル酸エチル、（メタ）アクリル酸ｎ−プロピル、（メタ）アクリル酸イソプロピル、（メタ）アクリル酸ｎ−ブチル、（メタ）アクリル酸イソブチル、（メタ）アクリル酸ｔ−ブチル、（メタ）アクリル酸ペンチル、（メタ）アクリル酸ヘキシル、（メタ）アクリル酸シクロヘキシル、（メタ）アクリル酸オクチル、（メタ）アクリル酸２−エチルヘキシル、（メタ）アクリル酸ノニル、（メタ）アクリル酸デシル、（メタ）アクリル酸ドデシル等、；炭素数６〜１２のアリール基又はアリールアルキル基を有する（メタ）アクリル酸エステルのモノマー、例えば（メタ）アクリル酸フェニル、（メタ）アクリル酸トルイル、（メタ）アクリル酸ベンジル等が挙げられる。
【００４１】
更に、他の（メタ）アクリル酸誘導体としてはヘテロ原子を含有する炭素数１〜２０のアルキル基を有する（メタ）アクリル酸エステルのモノマー、例えば（メタ）アクリル酸ヒドロキシエチル、（メタ）アクリル酸ジメチルアミノエチル、（メタ）アクリル酸ジエチルアミノエチル、（メタ）アクリル酸−２−アミノエチル、（メタ）アクリル酸−２−メトキシエチル、（メタ）アクリル酸−３−メトキシプロピル、（メタ）アクリル酸グリシジル、（メタ）アクリル酸エチレンオキサイドの付加物等；フッ素原子を含有する炭素数１〜２０のアルキル基を有する（メタ）アクリル酸エステルのモノマー、例えば（メタ）アクリル酸トリフルオロメチルメチル、（メタ）アクリル酸−２−トリフルオロメチルエチル、（メタ）アクリル酸−２−パーフルオロエチルエチル等；（メタ）アクリルアミド系モノマー、例えば（メタ）アクリルアミド、（メタ）アクリルジメチルアミド等が挙げられる。
【００４２】
モノオレフィンジカルボン酸としては、例えば、マレイン酸、クロロマレイン酸、シトラコン酸、イタコン酸、グルタコン酸、３−メチル−２−ペンテン・二酸（３−メチル−２−ペンテン−１，５−ジカルボン酸）、２−メチル−２−ペンテン・二酸、２−ヘキセン・二酸等が挙げられる。また、モノオレフィンジカルボン酸モノアルキルエステルとしては、炭素数１〜１２のアルキルアルコールとこれらのジカルボン酸とのモノエステルが挙げられ、アルキルアルコールとしては、具体的にはメチルアルコール、エチルアルコール、プロピルアルコール、ブチルアルコール、ペンチルアルコール、オクチルアルコール、シクロヘキシルアルコール等が挙げられる。
【００４３】
本発明の極性基含有プロピレン系重合体を用いて塗膜を形成した場合、塗膜と基材との塗膜密着性の面から、これらのグラフトするカルボキシル基等を含有する重合性単量体としては、溶解度パラメーターが高い方が好ましく、すなわち炭素数３〜１０の不飽和カルボン酸、その酸無水物およびそのエステルからなる不飽和カルボン酸誘導体成分が好ましい。特に無水マレイン酸が好ましい。
【００４４】
本発明で用いられる極性基含有プロピレン系重合体の内で、グラフト共重合単位としてモノオレフィンジカルボン酸モノアルキルエステルを有する変性重合体は、例えば、モノオレフィンジカルボン酸モノアルキルエステルを重合体にグラフト共重合する方法：モノオレフィンジカルボン酸もしくはその無水物を、プロピレン系重合体にグラフト共重合させた後に、アルキルアルコールによりカルボン酸基の１つをエステル化する方法によって得ることができる。
【００４５】
極性基含有プロピレン系重合体中におけるカルボキシル基等を含有する重合性単量体から選ばれる少なくとも１種のグラフト共重合単位のグラフト量、すなわち変性重合体中の含有量が、プライマーとして成型品に塗布して塗料の付着性が高い塗膜が得られ、また該塗膜と成型品との付着性も良好で、外観が良好となる点で０．０１〜２５重量％、好ましくは０．１〜１５重量％となるようにグラフト共重合する。
【００４６】
前記プロピレン系重合体にモノオレフィンジカルボン酸、その無水物およびモノオレフィンジカルボン酸モノアルキルエステル等の重合性単量体をグラフト共重合させる方法としては、種々の公知の方法が挙げられる。例えば、プロピレン系重合体を有機溶媒に溶解し、前記グラフトする重合性単量体およびラジカル重合開始剤を添加して加熱攪拌することによりグラフト共重合反応を行う方法；プロピレン系重合体を加熱して溶解し、該溶融物にグラフトする重合性単量体およびラジカル重合開始剤を添加し攪拌することによりグラフト共重合する方法；あるいは各成分を押出機に供給して加熱混練しながらグラフト共重合する方法；プロピレン系重合体のパウダーに前記グラフトする重合性単量体およびラジカル重合開始剤を有機溶媒に溶解した溶液を含浸させた後、パウダーが溶解しない温度まで加熱し、グラフト共重合する方法などが挙げられる。
【００４７】
このとき、ラジカル重合開始剤／グラフトする重合性単量体の使用割合は、通常モル比で１／１００〜３／５、好ましくは１／２０〜１／２の範囲である。反応温度は、５０℃以上、特に８０〜２００℃の範囲が好適であり、反応時間は２〜１０時間程度である。
【００４８】
上記グラフト共重合に用いられるラジカル重合開始剤としては、通常のラジカル開始剤から適宜選択して使用することができ、有機過酸化物、アゾニトリル等を挙げることができる。有機過酸化物としては、ジイソプロピルパーオキシド、ジ（ｔ−ブチル）パーオキシド、ｔ−ブチルヒドロパーオキシド、ベンゾイルパーオキシド、ジクミルパーオキシド、クミルヒドロパーオキシド、ジラウロイルパーオキシド、ジベンゾイルパーオキシド、メチルエチルケトンパーオキシド、シクロヘキサノンパーオキシド、クメンヒドロパーオキシド、ジイソプロピルパーオキシカルボナート、ジシクロヘキシルパーオキシカルボナート等が挙げられる。アゾニトリルとしてはアゾビスブチロニトリル、アゾビスイソプロピルニトリル等が挙げられる。これらの中で、ベンゾイルパーオキシド、ジクミルパーオキシドが好ましい。
【００４９】
上記グラフト共重合反応を有機溶媒を用いて行う場合、その有機溶媒の具体的な例としては、ベンゼン、トルエン、キシレン等の芳香族系炭化水素；ヘキサン、ヘプタン、オクタン、デカン等の脂肪族系炭化水素；トリクロロエチレン、パークロルエチレン、クロルベンゼン、ｏ−ジクロロベンゼン等のハロゲン化炭化水素などが挙げられ、これらの中でも、芳香族炭化水素もしくはハロゲン化炭化水素が好ましく、特にトルエン、キシレン、クロルベンゼンが好ましい。
【００５０】
本発明の変性プロピレン系重合体も変性前のプロピレン系重合体が可溶な前記の溶媒と同様の溶媒に溶解させることができる。本発明の変性プロピレン系重合体は、溶媒の中でも特に溶解度パラメーターが１１（ｃａｌ／ｃｍ³）^1/2以下の溶媒には溶解性が高いので、このプロピレン系重合体のグラフト変性体を溶解度パラメーターが１１（ｃａｌ／ｃｍ³）^1/2以下の溶剤に１重量％以上溶解した組成物は塗料組成物として有効である。
【００５１】
溶解度パラメーターが１１（cal/cm³）^1/2以下の溶媒の具体例としては、ベンゼン、トルエン、キシレン等の芳香族系炭化水素；ｎ−ペンタン、ｎ−ヘキサン、ｎ−ヘプタン、ｎ−オクタン、ｎ−デカン等の脂肪族系炭化水素；シクロヘキサン、メチルシクロヘキサン、ジメチルシクロヘキサン等の環式脂肪族系炭化水素、塩化メチレン、クロロホルム、四塩化炭素、トリクロロエチレン、パークロルエチレン、クロルベンゼン、ｏ−ジクロロベンゼン等のハロゲン化炭化水素、ｎ−メチルアセテート、ｎ−エチルアセテート、ｎ−ブチルアセテート等のエステル類、メチルイソブチルケトン、シクロヘキサノン等のケトン類、テトラヒドロフラン等のエーテル類などが挙げられ、これらの中でも、芳香族炭化水素もしくはハロゲン化炭化水素が好ましく、特にトルエン、キシレン、クロルベンゼンが好ましい。
【００５２】
本発明の塗料組成物は、塗料成分（Ａ）と該塗料成分（Ａ）を溶解する有機溶媒を主成分とするが、必要に応じて酸化防止剤、耐候安定剤、耐熱防止剤等の各種安定剤；酸化チタン、有機顔料等の着色剤、カーボンブラック、フェライト等の導電性付与剤等を含有していてもよい。
【００５３】
本発明の極性基含有プロピレン系重合体は、上述のように溶媒に可溶なので、結晶性を有するオレフィン系重合体の成形体に塗布することができる。これらのオレフィン系重合体のうち、プロピレン系重合体が好ましく用いられる。また、ポリプロピレンと合成ゴムとからなる成型品、ポリアミド樹脂、不飽和ポリエステル樹脂、ポリブチレンテレフタレート樹脂、ポリカーボネート樹脂等からなる成型品、例えば自動車用バンパー等の成型品、さらには鋼板や電着処理用鋼板等の表面処理にも用いることができる。さらに、ポリウレタン樹脂、脂肪酸変性ポリエステル樹脂、オイルフリーポリエステル樹脂、メラミン樹脂、エポキシ樹脂等を主成分とする塗料、プライマー、接着剤等を塗布した表面に下塗りし、その表面への塗料等の付着性を改善すると共に、鮮映性、低温衝撃性等にも優れる塗膜を形成するためにも用いることができる。
【００５４】
本発明の極性基含有プロピレン系重合体を含有する塗料成分（Ａ）を基材（Ｂ）に塗布した際に形成される塗膜は、基材に対して良好な密着性を示すので、基材に対する塗膜密着性樹脂として使用することができる。なお、基材に対して良好な密着性を得るためには、塗布後に加熱することが好ましい。加熱温度に特に制限はないが、実用性を考慮して５０〜１５０℃、さらには６０〜１３０℃とするのが好ましい。塗布の方法にも特に制限はなく、スプレーで塗布する方法、ローラーで塗布する方法、刷毛で塗布する方法など、従来公知の方法が使用できる。
【００５５】
本発明の極性基含有プロピレン系重合体を含有する塗料成分（Ａ）を塗布し、塗膜を形成した成形品の表面には、静電塗装、吹き付け塗装、刷毛塗り等の方法によって、塗料を塗布することができる。
塗料の塗布は、下塗りした後、上塗りする方法で行ってもよい。塗料を塗布した後、電熱、赤外線、高周波等によって加熱する通常の方法に従って塗膜を硬化させて、所望の塗膜を表面に有する成形品を得ることができる。塗膜を硬化させる方法は、成形品の材質、形状、使用する塗料の性状等によって適宜選ばれる。
【００５６】
極性基含有プロピレン系重合体を含有する塗料成分（Ａ）は、プライマー成分として用いることができる。すなわち、基材（Ｂ）の表面に塗布し、その表面への塗料の付着性や耐水性および耐ガソリン性といった塗膜性能を改善するためのプライマー成分として用いることができる。
具体的には、アクリル樹脂及び／又はポリエステル樹脂並びにポリウレタン変性ポリプロピレン樹脂と該極性基含有プロピレン系重合体とを、基材（Ｂ）へ塗布することができる。このようなプライマーは、塩素のようなハロゲンを含有せず、べたつき性がなく、溶解性にも優れ、かつアクリル樹脂及びポリエステル樹脂に対する相溶性に優れ、基材に対して良好な接着性、塗装性を保持し、耐水性、耐ガソホール性の高い塗膜を形成することが可能となる。
【００５７】
極性基含有プロピレン系重合体を含有する塗料成分（Ａ）は、プライマー成分の塗布が不要なベースカラー成分として用いることができる。すなわち、基材（Ｂ）の表面に塗布するに際し、基材の表面処理や洗浄を必要とせず、プライマー塗布が不要で、一回の塗装により良好な耐水性、耐候性を持つ塗膜が形成できるベースカラー成分として用いることができる。
【００５８】
このようなベースカラーは塩素のようなハロゲンを含有せず、べたつき性がなく、溶解性にも優れ、かつアクリルポリール及びポリエステルポリオールに対する相溶性に優れ、基材としての結晶性プロピレン系重合体等のポリオレフィンに対して良好な接着性、塗装性を保持し、耐久性、耐薬品性の高い塗膜を形成することが可能なであり、プライマー塗装が不要で、一回の塗装により良好な耐水性、耐候性を持つ塗膜が形成することができる。
【００５９】
なお、基材に対しプライマー成分を塗布し、塗膜の密着性をさらに改善することも可能である。
【００６０】
＜ＩＩ＞ 基材（Ｂ）成分
本発明に用いられる基材（Ｂ）は、結晶性ポリプロピレンの成形体である。ここに、結晶性ポリプロピレンとは、プロピレン単独重合体、及び／または、プロピレン単独重合体部とプロピレン・エチレン共重合体部からなるプロピレン・エチレンブロック共重合体からなる成形体である。
【００６１】
該プロピレン単独重合体、及びプロピレン・エチレンブロック共重合体のＭＦＲは好ましくは２ｇ／１０分以上、より好ましくは１０〜３００ｇ／１０分、特に好ましくは、２５〜２００ｇ／１０分である。
上記プロピレン・エチレンブロック共重合体及びプロピレン単独重合体のＭＦＲが２g／１０分未満であると流れ性が不十分となる傾向がある。逆に著しく高い場合、機械物性に劣るので好ましくない。
上記プロピレン・エチレンブロック共重合体のＭＦＲは、重合時に調整したもの、或いは重合後にジアシルパーオキサイド、ジアルキルパーオキサイド等の有機過酸化物で調整したものであってもよい。
【００６２】
プロピレン・エチレンブロック共重合体は、結晶性ポリプロピレン部（ａ単位部）とエチレン・プロピレンランダム共重合体部（ｂ単位部）とを含有するプロピレン・エチレンブロック共重合体である。
上記ａ単位部は、通常プロピレンの単独重合、場合によってはプロピレンに少量の他のα―オレフィンを共重合することによって得られる。
ａ単位部の、ポリプロピレン単独重合体のＭＦＲは、好ましくは１０g／１０分以上、より好ましくは１５〜５００g／１０分、さらに好ましくは、２０〜４００g／１０、特に好ましくは、４０〜３００g／１０分である。
上記プロピレン・エチレンブロック共重合体のプロピレン単独重合体部（ａ単位部）のＭＦＲが１０g／１０分未満であると流れ性が不十分となる傾向がある。逆にＭＦＲが著しく高い場合、機械物性に劣る傾向がある。
【００６３】
一方、上記ｂ単位部はプロピレンとエチレンとのランダム共重合によって得られるゴム状成分である。
上記プロピレン・エチレン共重合体部（ｂ単位部）のプロピレン含量は、好ましくは３０〜８５重量％、より好ましくは４０〜８０重量％、さらに好ましくは５０〜７５重量％である。共重合体部のプロピレン含量が上記範囲を逸脱した場合、その分散性が悪化したり、ガラス転移温度が上昇するなど、衝撃特性の悪化する傾向がある。
プロピレン・エチレン共重合体部のプロピレン含量は、プロピレン・エチレン共重合体部の重合時にプロピレンとエチレンの濃度比を制御することにより、調整することができる。
【００６４】
また、上記プロピレン・エチレン共重合体部の分子量については、特に制約はないが、分散性や耐衝撃性を考慮し、重量平均分子量（Ｍｗ）は、好ましくは２０万〜３００万、より好ましくは３０万〜２５０万、さらに好ましくは４０万〜２００万である。
【００６５】
ａ単位部、ｂ単位部の量については特に制限はないが、一般にａ単位部は、好ましくは全重合量の９５重量％以下、より好ましくは５０〜９５重量％、さらに好ましくは６０〜９０重量％、ｂ単位部は、好ましくは全重合量の５重量％以上、より好ましくは５〜５０重量％、さらに好ましくは１０〜４０重量％となるように調整される。
ｂ単位部の量が、上記範囲未満であると、ブロック共重合体として期待される耐衝撃特性が不十分となる傾向があり、上記範囲を超えると剛性、強度及び耐熱性が不足する傾向があり好ましくない。
【００６６】
本発明において、この共重合体部の量は、昇温溶出分別法を用いて測定するものとする。すなわちａ単位部は、オルトジクロロベンゼンによる抽出において、１００℃以下で溶出しないが、ｂ単位部は容易に溶出する。従って、製造後の重合体に対して、上記したオルトジクロロベンゼンによる抽出分析によりプロピレン・エチレンブロック共重合体の組成を判定するものとする。
プロピレン・エチレン共重合体部の量は、プロピレン単独重合体部の重合量とプロピレン・エチレン共重合体部の重合量の比率を重合時間などにより制御し、調整することができる。
【００６７】
プロピレン単独重合体、及び／または、プロピレン単独重合体部とプロピレン・エチレン共重合体部からなるプロピレン・エチレンブロック共重合体の製造法は特に限定されるものではなく、公知の方法、条件の中から適宜に選択される。
プロピレンの重合触媒としては、通常、高立体規則性触媒が用いられる。例えば、四塩化チタンを有機アルミニウム化合物で還元し、更に各種の電子供与体及び電子受容体で処理して得られた三塩化チタン組成物と有機アルミニウム化合物及び芳香族カルボン酸エステルを組み合わせた触媒（特開昭５６―１００８０６号、特開昭５６−１２０７１２号、特開昭５８−１０４９０７号の各公報参照）、及び、ハロゲン化マグネシウムに四塩化チタンと各種の電子供与体を接触させた担持型触媒（特開昭５７−６３３１０号、同６３−４３９１５号、同６３−８３１１６号の各公報参照）等を例示することができる。さらに、ＷＯ−９１／０４２５７号公報等に示されるようなメタロセン系触媒が挙げられる。なお、メタロセン系触媒と称せられる触媒は、アルモキサンを含まなくてもよいが、好ましくはメタロセン化合物とアルモキサンとを組み合わせた触媒、いわゆるカミンスキー系触媒のことである。
【００６８】
プロピレン・エチレンブロック共重合体は、上記触媒の存在下、気相重合法、液相塊状重合法、スラリー重合法等の製造プロセスを適用して、プロピレンを単独で重合し、続いてプロピレンとエチレンをランダム重合することにより得られる。上記した溶融特性（ＭＦＲ）等を有するプロピレン・エチレンブロック共重合体を得るためには、スラリー法、気相流動床法にて、多段重合することが好ましい。プロピレンの単独重合を多段で行い、続いてプロピレンとエチレンをランダム重合する方法で得ることもできる。ｂ単位部の多いプロピレン・エチレンブロック共重合体の製造においては、特に気相流動床法が好ましい。
【００６９】
プロピレン単独重合体は、上記触媒の存在下、気相重合法、液相塊状重合法、スラリー重合法等の製造プロセスを適用して、プロピレンを単独で重合することにより得られる。上記した溶融特性（ＭＦＲ）を有するプロピレン単独重合体を得るためには、スラリー法、気相流動床法にて、多段重合することが好ましい。
【００７０】
本発明のプロピレン・エチレンブロック共重合体及びプロピレン単独重合体の機械的物性は、曲げ弾性率が好ましくは３００ＭＰａ以上 より好ましくは５００〜３０００ＭＰａ、さらに好ましくは１０００〜２０００ＭＰａである。前記範囲外であると、剛性感に劣り、構造材料として適さない。
ＩＺＯＤ衝撃強度は好ましくは１ｋＪ／ｍ²以上、より好ましくは２〜１００ｋＪ／ｍ²、さらに好ましくは５〜８０ｋＪ／ｍ²、特に好ましくは８〜６０ｋＪ／ｍ²の範囲が好ましい。前記範囲未満であると、耐衝撃特性に劣り、構造材料として適さない。
【００７１】
本発明の基材（Ｂ）がタルク、亜鉛華、ガラス繊維、チタン白、硫酸マグネシウム等の無機充填剤、顔料等が配合されている場合にも、特に付着性の良い塗膜を形成することができる。
【００７２】
また、本発明の基材（Ｂ）は、上記以外に、本発明の効果を著しく損なわない範囲で、任意の添加剤や配合成分を含有することができる。
具体的には、着色するための顔料、フェノール系、イオウ系、リン系などの酸化防止剤、帯電防止剤、ヒンダードアミン等光安定剤、紫外線吸収剤、各種造核剤、分散剤、中和剤、発泡剤、銅害防止剤、滑剤、難燃剤、上記プロピレン系ブロック共重合体以外の各種樹脂、ポリブタジエン、ポリイソプレン等各種ゴム成分等の配合材を挙げることができる。
【００７３】
詳しくは、ペンタエリスチル−テトラキス［３−（３，５−ジ−ｔ−ブチル−４−ヒドロキシルフェニル）プロピオネート］、オクタデシル−３−（３，５−ジ−ｔ−ブチル−４−ヒドロキシフェニル）プロピオネート、トリス−（３，５−ジ−ｔ−ブチル−４−ヒドロキシベンジル）−イソシアヌレート、トリエチレングリコール−ビス［３−（３−ｔ−ブチル−５−メチル−４−ヒドロキシルフェニル）プロピオネート］等のフェノール系酸化防止剤、トリス（２，４−ジ−ｔ−ブチルフェニル）フォスファイト、ビス（２，４−ジ−ｔ−ブチルフェニル）ペンタエリスリトールジフォスファイト、テトラキス（２，４−ジ−ｔ−ブチルフェニル）−４，４’−ビフェニレンジフォスフォナイト等のリン系酸化防止剤、ジミリスチル−３，３’−チオジプロピオネート、ジステアリルチオジプロピオネート、２−（３−ｔ−ブチル−５−メチル−２−ヒドロキシフェニル）−５−クロロベンゾトリアゾール、２−（３，５−ジ−ｔ−ブチル−２−ヒドロキシフェニル）ベンゾトリアゾール、２−ヒドロキシ−４−ｎ−オクチルオキシベンゾフェノン等の紫外線吸収剤、ビス（２，２，６，６−テトラメチル−４−ピペリジル）セバケート、ビス（１，２，２，６，６−ペンタメチル−４−ピペリジル）セバケート、ポリ［｛６−（１，１，３，３−テトラメチルブチル）アミノー１，３，５−トリアジン−２，４−ジイル｝｛（２，２，６，６−テトラメチル−４−ピペリジル）イミノ｝ヘキサメチレン｛（２，２，６，６−テトラメチル−４−ピペリジル）イミノ｝］、ビス（１−オクチル−２，２，６，６−テトラメチル−４−ピペリジル）セバケート、テトラキス（２，２，６，６−テトラメチル−４−ピペリジル）１，２，３，４−ブタンテトラカーボキシレート、テトラキス（１，２，２，６，６−ペンタメチル−４−ピペリジル）１，２，３，４−ブタンテトラカーボキシレート、２，４−ジ−ｔ−ブチルフェニル−３，５−ジ−ｔ−ブチル−４−ヒドロキシベンゾエート等の耐候安定剤、グリセリルモノステアレート等の帯電防止剤を例示できる。
【００７４】
本発明の基材（Ｂ）を構成するプロピレン系樹脂組成物の製造方法は特に限定されず、従来公知の方法で、必要に応じて、上記配合成分をプロピレン系樹脂へ配合し、混合及び溶融混練することにより製造することができる。
【００７５】
本発明においては、上述した必須成分、すなわち、プロピレン単独重合体、及び／又はプロピレン単独重合体部とプロピレン・エチレン共重合体部からなるプロピレン・エチレンブロック共重合体、並びに必要に応じて用いられる任意成分等を、上記配合割合で配合して、一軸押出機、二軸押出機、バンバリーミキサー、ロールミキサー、ブラベンダープラストグラフ、ニーダー等の通常の混練機を用いて混練・造粒することによって、本発明の基材（Ｂ）を構成するプロピレン系樹脂組成物が得られる。
【００７６】
この場合、各成分の分散を良好にすることができる混練・造粒方法を選択することが好ましく、通常は二軸押出機を用いて行われる。この混練・造粒の際には、上記各成分の配合物を同時に混練してもよく、また性能向上をはかるべく各成分を分割して混練する方法を採用することもできる。
【００７７】
本発明の基材（Ｂ）は、結晶性ポリプロピレンを使用し、公知の各種方法による成形により得ることができる。例えば射出成形（ガス射出成形も含む）、圧縮成形、射出圧縮成形（プレスインジェクション）、押出成形、中空成形、回転成形、カレンダー成形、インフレーション成形、一軸延伸フィルム成形、二軸延伸フィルム成形等にて成形することによって各種成形体を得ることができる。このうち、射出成形、圧縮成形、射出圧縮成形による成形体が好ましい。
【００７８】
本発明の塗装されたプロピレン系樹脂成形体は、塩素などのハロゲンを含有しないため環境負荷が少なく、塗膜密着性に優れ、さらに剛性、耐衝撃性に優れた物性バランスを有するものである。
本発明の塗装されたプロピレン系樹脂成形体は、各種工業部品分野、特に薄肉化、高機能化、大型化された各種成形品、例えばバンパー、インストルメントパネル、トリム、ガーニッシュなどの自動車部品、テレビケース、洗濯機槽、冷蔵庫部品、エアコン部品、掃除機部品などの家電機器部品、便座、便座蓋、水タンクなどのトイレタリー周りの部品、浴槽、浴室の壁、天井などの部品、排水パンなどの浴室周りの部品などの各種工業部品用成形材料として、実用に十分な性能を有している。
【００７９】
【実施例】
次に実施例及び比較例によって本発明をさらに具体的に説明するが、本発明はその要旨を逸脱しない限りこれら実施例によって制約を受けるものではない。
なお、以下の実施例及び比較例において重合体の物性・性能測定は次の通り行った。また、各例において、触媒合成工程および重合工程は、全て精製窒素雰囲気下で行い、溶媒は、モレキュラーシーブ（ＭＳ−４Ａ）で脱水した後に、精製窒素でバブリングして脱気して使用した。
【００８０】
（１）分子量
クロマト分析装置（ウオーターズ社製ＧＰＣ１５０ＣＶ型）を使用した。溶媒としてオルトジクロロベンゼンを使用し、測定温度は１３５℃とした。分子量算出は、標準試料として市販の単分散のポリスチレンを使用し、該ポリスチレン標準試料およびポリプロピレンの粘度式から、保持時間と分子量に関する校正曲線を作成し分子量の算出を行った。
【００８１】
（２）プロピレン単位連鎖部のペンタッド
試料３５０〜５００ｍｇを、１０ｍｍφのＮＭＲ用サンプル管中で、約２．２ｍｌのオルトジクロロベンゼンを用いて完全に溶解させる。次いで、ロック溶媒として約０．２ｍｌの重水素化ベンゼンを加え、均一化させた後、１３０℃でプロトン完全デカップリング法により測定を行う。測定条件は、フリップアングル９０°、パルス間隔５Ｔ１以上（Ｔ１は、メチル基のスピン−格子緩和時間のうち最長の値）とする。プロピレン重合体において、メチレン基およびメチン基のスピン−格子緩和時間はメチル基のそれよりも短いので、この測定条件では、すべての炭素の磁化の回復は９９％以上である。なお、定量精度を上げるため、¹³Ｃ核の共鳴周波数として１２５ＭＨｚ以上のＮＭＲ装置を使用し、２０時間以上の積算を行うのが好ましい。
【００８２】
（３）結晶化度
広角×線結晶回折により測定し、多重ピーク分離法により決定した（対称透過法（２θ／θ＝５〜６０゜、０．１゜／ｓｔｅｐ））。
（４）融点及び結晶融解熱
融点Ｔｍおよび結晶融解熱はＤｕＰｏｎｔ社製熱分析システムＴＡ２０００を使用して、以下の方法で求めた。
試料（約５〜１０ｍｇ）を精秤し専用のアルミパンに入れる。２００℃で３分間融解後、１０℃／分の速度で３０℃まで降温した後に、１０℃／分で２００℃まで昇温することにより融解曲線を得て、最後の昇温段階における主吸熱ピークのピークトップ温度を融点として求めた。またそのピークとベースラインで囲まれた面積から算出される熱量を試料の重量で割ったものを結晶融解熱量（Ｊ/g）とする。融解曲線の５０〜１６０℃の温度域において、１Ｊ／ｇ以上に相当する明確なピークが存在しない場合、ｎ．ｄ．として表した。
【００８３】
（５）オルトジクロロベンゼンによる昇温溶出分別
溶出分別装置（三菱化学社製ＣＦＣ−Ｔ−１０２Ｌ）を用いて、１００％溶出温度として求めた。溶出分別は５℃から開始し、４〜５℃刻みで昇温して測定した。
（６）溶解性試験
溶剤（ヘプタン又はトルエン）に試料を濃度１０重量％で攪拌翼付きセパラブルフラスコに仕込み、ヘプタンは外温１１０℃、トルエンは外温１２０℃に昇温し溶解する。内温が一定となった後２時間攪拌を続ける。ヘプタンは沸騰時の温度で素早く、トルエンは３０℃まで自然冷却してから、溶液温度を２５℃に調節して１時間静置し、ＳＵＳ金網４００番にてろ過する。金網に残ったものを不溶分、溶液として通ったものを可溶分とし、真空乾燥器で８０℃、１ｍｍＨｇ以下、４時間乾燥させる。秤量し、不溶分の分率を計算する。

【００８４】
（７）ノンタック性
指触タック性試験により下記基準で評価した。

（８）曲げ弾性率
型締め圧１００トンの射出成型機を用いて、金型温度４０℃、シリンダー温度２２０℃にて射出成形により９０mm×１０mm×３ｍｍの試験片を成形し、得られた射出成形片について、ＪＩＳ−Ｋ７２０３に準拠して試験速度２ｍｍ／分、２３℃下で測定（単位：Ｍｐａ）した。
（９）アイゾット（ＩＺＯＤ）衝撃強度
同上試験片について、ＪＩＳ−Ｋ７１１０に準拠して２３℃下で測定（単位：ｋＪ／ｍ²）した。
【００８５】
（１０）層間密着性試験
日本ポリケム社製ポリプロピレンを、射出成型機（東芝機械社製ＩＳ１７０）を用いて、成形温度２２０℃の設定で、１５０mm×７０mm×２mmの試験片を成形した。
後述の方法で塗膜を形成した後、ＪＩＳ−Ｋ５４００に記載されている碁盤目試験の方法に準じて、碁盤目を付けた試験片を作成し、粘着テープ（ニチバン社製、登録商標セロテープ）を、試験片の碁盤目上に張り付けた後、これを速やかに垂直方向に引っ張って剥離させ、碁盤目１００個のうちで剥離されなかった碁盤目の数を数え「残留碁盤目数／100個」で表記した。
（１１）耐水性試験
塗料成分（Ａ）またはそれ以外のポリマーをプライマーとして基材上に塗膜を形成し、その塗膜の上からベースコートを塗装して焼き付け、室温にて養生した塗装物を４０℃に保った温水中に１０日間浸漬する。その後、表面の水分を乾燥させた後、前記層間密着性試験と同様にして碁盤目試験（ＪＩＳ−Ｋ５４００）に準じた密着性試験を行った。
【００８６】
（１２）耐ガソホール性試験
塗料成分（Ａ）またはそれ以外のポリマーをプライマーとして基材上に塗膜を形成し、その塗膜の上からベースコートを塗装して焼き付け、室温にて養生した塗装物を２０℃に保ったレギュラーガソリン：エタノール＝９：１混合溶液中に浸漬してその塗膜に顕著な剥離が生じるまでの時間を測定した。
【００８７】
［製造例１］
（１） ジクロロ［ジメチルシリレン（シクロペンタジエニル）（２，４−ジメチル−４Ｈ−１−アズレニル）ハフニウムの合成
（１）−１ 配位子の合成
２−メチルアズレン（４．０１ｇ）をテトラヒドロフラン（５６ｍｌ）に溶解し、アイスバスにて０℃に冷却した後、同温度でメチルリチウムのジエチルエーテル溶液（１．１４ｍｏｌ／ｌ）２４．８ｍｌを滴下した。滴下終了後、アイスバスを外して２時間攪拌した。この溶液を、アイスバスにて０℃に冷却したジメチルシリルジクロリド（３４．０ｍｌ， ０．２８０ｍｏｌ）のテトラヒドロフラン溶液（１４０ｍｌ）にゆっくり滴下した。滴下終了後、アイスバスを外して３時間攪拌した後、減圧下に溶媒および未反応のジメチルシリルジクロリドを留去した。テトラヒドロフラン（８０ｍｌ）を加えて０℃まで冷却し、シクロペンタジエニルナトリウム（２．１ｍｏｌ／ｌ， ２６．９ｍｌ， ５６．５ｍｍｏｌ）を徐々に滴下し、滴下終了後、室温で１２時間撹拌した。攪拌終了後、水を加え、ジエチルエーテルで目的とする化合物を抽出した。抽出溶液を硫酸マグネシウムで脱水した後、乾固することにより目的配位子の未精製品を得た。ｎ−ヘキサンを溶出溶媒とするシリカゲルカラムクロマトグラフィーで、該未精製品を精製することにより、目的の配位子（６．２９ｇ）を収率７９％で得た。
【００８８】
（１）−２ 錯体の合成
（１）−１で得られた配位子（６．２９ｇ）をテトラヒドロフラン（１００ｍｌ）に溶解し、アイスバスにて０℃に冷却した。ここに同温度で、ｎ−ブチルリチウムのｎ−ヘキサン溶液（１．５６ｍｏｌ／ｌ， ２８．４ｍｌ）を、ゆっくり滴下した。滴下終了後、アイスバスをはずして３時間攪拌し、減圧下に溶媒を留去した。留去後得られた残渣にトルエン（６０ｍｌ）を加えた後、−７８℃に冷却した。ここに、−７８℃に冷却したハフニウムテトラクロリド（７．１７ｇ）のトルエン（１４０ｍｌ）懸濁液をゆっくり添加した。その後、冷却浴をはずして終夜攪拌した。攪拌終了後、反応液をＧ３フリットを用いて濾過した。フリット上の固体をさらにトルエンで洗浄し、濾液を濃縮することにより、褐色の粉末が得られた。この褐色の粉末から、ホットｎ−ヘキサン（１８０ｍｌ×３回）で目的錯体を抽出した。抽出溶液を乾固させた後、得られた固体をｎ−ヘキサン（２０ｍｌ×５回）で懸濁洗浄した後、減圧下で乾燥させることにより、目的とするジクロロ［ジメチルシリレン（シクロペンタジエニル）（２，４−ジメチル−４Ｈ−１−アズレニル］ハフニウム（２．９０ｇ）を得た（収率２５％）。
上記化合物の¹H-NMR測定した結果を以下に示す。
¹H-NMR(CDCl₃):δ0.85(s,3H),0.86(s,3H),1.47 (d,J = 7.1 Hz, 3H), 2.25 (s,3H), 3.42-3.52 (m,1H), 5.42 (dd,J = 4.7, 10.1 Hz,1H), 5.80-5.85 (m,2H), 5.90-5.95 (m, 1H), 6.16-6.20 (m,2H), 6.65 (d,J = 11.4H), 6.80-6.85 (m,1H), 6.98-7.02 (m,1H)。
【００８９】
（２）粘土鉱物の化学処理
１，０００ｍｌ丸底フラスコに、脱塩水（１１０ｍｌ）、硫酸マグネシウム・７水和物（２２．２ｇ）および硫酸（１８．２ｇ）を採取し、攪拌下に溶解させた。この溶液に、造粒モンモリロナイト（水澤化学社製ベンクレイＳＬ）１６．７ｇを分散させ、２時間かけて１００℃まで昇温し、１００℃で２時間攪拌を行った。その後、１時間かけて室温まで冷却し、得られたスラリーを濾過してウェットケーキを回収した。回収したケーキを１，０００ｍｌ丸底フラスコにて、脱塩水（５００ｍｌ）にて再度スラリー化し、濾過を行った。この操作を２回繰り返した。最終的に得られたケーキを、窒素雰囲気下１１０℃で終夜乾燥し、化学処理モンモリロナイト（１３．３ｇ）を得た。
【００９０】
（３）重合
（２）で得られた化学処理モンモリロナイト（０．４４ｇ）に、トリエチルアルミニウムのトルエン溶液（０．４ｍｍｏｌ／ｍｌ， ２．０ｍｌ）を加え、室温で１時間攪拌した。この懸濁液にトルエン（８ｍｌ）を加え、攪拌後、上澄みを除いた。この操作を２回繰り返した後、トルエンを加えて、粘土スラリー（スラリー濃度＝９９ｍｇ粘土／ｍｌ）を得た。
別のフラスコに、トリイソブチルアルミニウム（東ソー・アクゾ社製）０．１１４ｍｍｏｌを採取し、ここで得られた粘土スラリー（３．８ｍｌ）および製造例１（１）−２で得られた錯体（６．０２ｍｇ， １１．４μｍｏｌ）のトルエン希釈液を加え、室温で１０分間撹拌し、触媒スラリーを得た。
【００９１】
次いで、内容積２リッターの誘導攪拌式オートクレーブ内に、トルエン（７５０ｍｌ）、トリイソブチルアルミニウム（１．９ｍｍｏｌ）および液体プロピレン（１８０ｍｌ）を導入した。室温で、上記触媒スラリーを全量導入し、６０℃まで昇温し重合時の全圧を０．７ＭＰａで一定に保持しながら、同温度で１時間攪拌を継続した。攪拌終了後、未反応プロピレンをパージして重合を停止した。オートクレーブを開放してポリマーのトルエン溶液を全量回収し、溶媒ならびに粘土残渣を除去したところ、２３．２ｇのプロピレン重合体が得られた。得られた重合体を分析した結果を表１にまとめて示す。表中、「n.d.」は非検知（not detected）を表す。
【００９２】
［製造例２］
粘土スラリー用物質として、錯体を１７．８ｍｇ（３４．２ｍｍｏｌ）、トリイソブチルアルミニウム（０．３４２ｍｍｏｌ）、粘土スラリー（１１．４ｍｌ）を用い、またトルエン（１１００ｍｌ）、トリイソブチルアルミニウム（０．５ｍｍｏｌ）、液体プロピレン（２６４ｍｌ）、重合時の温度を８０℃、全圧を０．８Ｍｐａ、重合時間を１．８３時間とした以外は全て製造例１と同様の操作にて行った。その結果、２４５ｇのプロピレン重合体が得られた。得られた重合体を分析した結果を表１にまとめて示す。
【００９３】
［製造例３］
トルエン（１３５０ｍｌ）、液体プロピレン（９０ｍｌ）、重合時の温度を７０℃、全圧を０．３１Ｍｐａ、重合時間を２時間とした以外は全て製造例２と同様の操作にて行った。その結果、４４ｇのプロピレン重合体が得られた。得られた重合体を分析した結果を表１にまとめて示す。
【００９４】
［製造例４］
液体プロピレン（１８２ｍｌ），トリイソブチルアルミニウム（０．５ｍｍｏｌ）とした以外は全て製造例１と同様の操作にて行った。その結果、３９．６ｇのプロピレン重合体が得られた。得られた重合体を分析した結果を表１にまとめて示す。
【００９５】
［製造例５］
（１）ジクロロ｛１，１’−ジメチルシリレンビス［２−エチル−４−（２−フルオロ−４−ビフェニリル）−４Ｈ−アズレニル］｝ハフニウムのラセミ体の合成
２−フルオロ−４−ブロモビフェニル（６．３５ｇ，２５．３ｍｍｏｌ）を、ジエチルエーテル（５０ｍｌ）とｎ−ヘキサン（５０ｍｌ）の混合溶媒に溶かし、ｔ−ブチルリチウムのｎ−ペンタン溶液（３３ｍｌ，５０．６ｍｍｏｌ，１．５４Ｎ）を−７８℃で滴下した。−１０℃で２時間攪拌し、この溶液に２−エチルアズレン（３．５５ｇ，２２．８ｍｍｏｌ）を加え、室温で２時間攪拌した。ｎ−ヘキサン（３０ｍｌ）を加え、上澄みをデカンテーションで除去した。さらに、この操作をもう一度繰り返した。得られた黄色沈殿に、０℃でｎ−ヘキサン（３０ｍｌ）とテトラヒドロフラン（４０ｍｌ）を加えた。次いで、Ｎ−メチルイミダゾール（５０ｍｌ）とジメチルジクロロシラン（１．４ｍｌ，１１．４ ｍｍｏｌ）を加え、室温まで昇温し、室温で１時間攪拌した。この後、希塩酸を加え、分液した後有機相を硫酸マグネシウムで乾燥し、減圧下に溶媒を留去すると、ジメチルシリレンビス（２−エチル−４−（２−フルオロ−４−ビフェニル）−１，４−ジヒドロアズレン）の粗生成物（８．３ｇ）が得られた。
【００９６】
次に、上記で得られた粗生成物をジエチルエーテル（３０ｍｌ）に溶かし、−７０℃でｎ−ブチルリチウムのｎ−ヘキサン溶液（１４．９ｍｌ，２２．８ｍｍｏｌ， １．５３Ｎ）を滴下し、徐々に昇温して、室温で一夜攪拌した。さらに、トルエン（２００ｍｌ）を加え、−７０℃に冷却し、四塩化ハフニウム（３．６ｇ，１１．４ｍｍｏｌ）を加え、徐々に昇温し、室温で４時間攪拌した。得られたスラリーから、減圧下に大部分の溶媒を留去し、ジエチルエーテル（５０ｍｌ）を加え、得られたスラリーを濾過した。ジエチルエーテル（５ｍｌ×２）、エタノール（１５ｍｌ×２）、ｎ−ヘキサン（１０ｍｌ×２）で洗浄すると、ジクロロ｛１，１’−ジメチルシリレンビス［２−エチル−４−（２−フルオロ−４−ビフェニリル）−４Ｈ−アズレニル］｝ハフニウムのラセミ・メソ混合物（４．５３ｇ，収率４２％）が得られた。得られたラセミ・メソ混合物を¹Ｈ−ＮＭＲで分析した結果、ラセミ体７６．６％、メソ体２３．４％の混合物であることがわかった。
ここで得られたラセミ・メソ混合物（４．５ｇ）をジクロロメタン（３５ｍｌ）に懸濁し、高圧水銀灯（１００Ｗ）を用いて１時間光照射した。減圧下に溶媒を留去し、得られた固体にトルエン（２５ｍｌ）とジクロロメタン（１１ｍｌ）を加え、６０℃に加熱すると均一溶液となった。減圧下にジクロロメタンを留去すると結晶が析出した。得られた結晶を濾過して、ヘキサン（５ｍｌ）で２回洗浄し、減圧下乾燥すると、ラセミ体（１．７９ｇ）が得られた。
【００９７】
（２） 粘土鉱物の化学処理
５００ｍｌ丸底フラスコに、脱塩水５５．８５ｇと硫酸３２．７０ｇおよび水酸化リチウム８．０１ｇを加えて攪拌した後、モンモリロナイト（水澤化学製：水澤スメクタイト）５１．６５ｇを添加し、昇温して還流下に１４０分間処理した。脱塩水３００ｍｌを加えて吸引濾過した後、脱塩水６００ｍｌに固体成分を分散させて吸引濾過した。この操作をさらにもう１度繰り返した。濾過して得られた残留物を１００℃で乾燥し、酸および金属塩処理モンモリロナイトを得た。
ここで得られた酸および金属塩処理モンモリロナイト１．０５ｇを１００ｍｌ丸底フラスコに採取し、減圧下、２００℃で２時間加熱乾燥させた。これに、トリエチルアルミニウムのトルエン溶液（０．５ｍｍｏｌ／ｍｌ）を、精製窒素下で４．０ｍｌ添加して、室温で３０分反応させた後、トルエン３０ｍｌで２回洗浄し、化学処理モンモリロナイトを含有するトルエンスラリーを得た。
【００９８】
（３） 予備重合
（２）で得られたトルエンスラリー（固形分として９１４．２ ｍｇ含有）からトルエンを抜き出し、残存トルエン量を１．０ｍｌとした。このスラリーに、トリイソブチルアルミニウムのトルエン溶液（０．５ｍｍｏｌ／ｍｌ，０．５ｍｌ）を加え、さらに、（１）で合成したジクロロ｛１，１’−ジメチルシリレンビス［２−エチル−４−（２−フルオロ−４−ビフェニリル）−４Ｈ−アズレニル］｝ハフニウムのラセミ体のトルエン溶液（３．０ｍｍｏｌ／ｍｌ，９．２ｍｌ）を加え、室温で１時間攪拌し、触媒スラリーを得た。
２リッターの誘導攪拌式オートクレーブに、精製窒素下、トルエン４０ｍｌと上記触媒スラリー全量を導入した。攪拌下にプロピレン１１．０ ｇを導入し、３０℃で２時間、次いで５０℃で０．５時間予備重合を行った。予備重合後、未反応のプロピレンをパージし、精製窒素０．５ＭＰａで２回加圧置換した後予備重合触媒を取り出した。このものは、化学処理モンモリロナイト成分１ｇあたり９．７ｇの重合体を含有していた。
【００９９】
（４） 重合
いかり型攪拌翼を内蔵する２リッターの誘導攪拌式オートクレーブを精製窒素で置換し、次いで、２５℃で液化プロピレン７５０ｇを装入した。トリイソブチルアルミニウムのトルエン溶液（０．１ｍｍｏｌ／ｍｌ，５．０ｍｌ）を同温度で圧入後、７０℃まで昇温した。水素を、気相中の水素濃度で０．２ｍｏｌ％になるように加えた後、７０℃で、上記（３）で得られた予備重合触媒を３０．０ｍｇ加え、重合を開始した。１時間後、未反応のプロピレンをパージし、重合を終了した。得られたプロピレン重合体の量は３８４ｇであった。
【０１００】
得られた重合体を分析した結果を表１に纏めて示す。
なお、¹³Ｃ−ＮＭＲによる頭−尾結合からなるプロピレン単位連鎖部のメチル基の炭素原子に由来するピーク：［ｍｍｍｍ］＞９９．９（％）であり、他のペンタッドに由来するピークはほとんど見られなかった。
【０１０１】
［製造例６］
内容積５０ｍＬの誘導攪拌式ミクロオートクレーブ内に、高立体特異性アイソタクチックポリプロピレン（３１．１ｇ）、ヘプタン（１８０ｍｌ）、Ｐｄ／Ｃ（アルドリッチ社：１０重量％Ｐｄ／Ｃ）（７．８７ｇ）を加えた後、系を密閉系にし、窒素置換を行った。その後、水素を８．０ＭＰａ導入し、２７５℃まで昇温して、６時間攪拌を継続した。冷却後、水素をパージして反応を停止した。オートクレーブを開放してポリマーのヘプタン溶液を全量回収し、溶媒ならびにＰｄ／Ｃ残渣を除去したところ、３０．６ｇのプロピレン重合体が得られた。
なお、使用した高立体特異性アイソタクチックポリプロピレンの物性は、次の通りである。
ＭＦＲ：１５，０００ｇ／１０分；
Ｔｍ：１５４．９℃；
Ｍｗ：３７，０００；Ｍｎ：１８，０００；Ｍｗ／Ｍｎ：２．１；
［ｍｍｍｍ］：９８．４％；［ｍｍｍｒ］：０．０％；［ｒｍｒｍ］：０．１％；［ｒｒｒｒ］：０．２％。
【０１０２】
［参考例１］
チーグラー・ナッタ系ポリプロピレン（宇部興産社製、ウベタックＵＴ−２１１５）の物性を同様に測定した。
【０１０３】
以下の実施例において、基材（Ｂ）として使用した結晶性ポリプロピレンのグレード名、タイプ、物性値等を表２に示した.グレード名はいずれも日本ポリケム社の商品名である。なお、表２中、ペンタッド分率はｍｍｍｍペンタッドを指す。
【０１０４】
【表１】

【０１０５】
【表２】

【０１０６】
［実施例１］
（１） プロピレン重合体の無水マレイン酸変性
温度計、攪拌機のついたステンレス耐圧反応容器中に、クロロベンゼン（８０ｇ）、製造例１（３）で得られたプロピレン重合体（２０ｇ）および無水マレイン酸（４ｇ）を加え、容器内を窒素ガスで置換し、１３２℃に昇温した。昇温後、ジクミルペルオキシド（DCPO）のクロロベンゼン溶液（１０重量％）１６ｇを、定量ポンプを用いて５時間で供給した後、３時間同温度で攪拌を続けて反応を行った。反応終了後、系を室温付近まで冷却し、アセトンを加えて、沈殿したポリマーを濾別した。さらにアセトンで沈殿・濾別を繰り返し、最終的に得られたポリマーをアセトンで洗浄した。洗浄後に得られたポリマーを減圧乾燥することにより、白色粉末状の変性樹脂が得られた。この変性樹脂の赤外線吸収スペクトル測定および中和滴定等を行った結果、グラフト量（無水マレイン酸基の含量）は、３．３重量％であった。
ここで得られた無水マレイン酸変性プロピレン重合体１５ｇにトルエン１３５ｇを加え、１００℃に昇温し、１時間かけて溶解させた。得られた溶液を室温付近まで冷却した後、＃４００のＳＵＳ金網を通して、無水マレイン酸変性プロピレン重合体の１０重量％溶液を調製した。
【０１０７】
（２） 変性プロピレン重合体の物性評価
表２に示す各種のＰＰ基材で作成した射出成形試験片（イソプロピルアルコールで表面を清拭したもの）に、上記（１）で得られた無水マレイン酸変性プロピレン重合体のトルエン溶液を塗布量３〜５ｇ／ｍ²で噴霧塗布した。次にこの成形試験片を２５℃にて１時間静置した後、セーフベンドライヤー中にて８０℃、３０分間乾燥させた。次いで、この乾燥品を２５℃にて１時間静置させた後、その塗膜の上からベースコートとしてアクリルポリオールウレタン塗料（関西ペイント社製：商品名レタンＰＧ８０III）を、所定量の硬化剤と配合して、フォードカップ４番にて専用シンナーで粘度調整を行い、粘度が１２〜１３秒となるように調整した後、乾燥塗布量が５０〜６０ｇになるように噴霧塗装し、セーフベンドライヤー中にて１００℃、３０分間焼き付けを行った。さらに、２５℃にて１０日間静置し養生した。得られた塗装物について層間密着性試験を行った。また、耐水性試験及び耐ガソホール性試験も行った。その結果を以下の実施例と纏めて表３に示す。
【０１０８】
［実施例２］
トルエン（８０ｇ）、製造例２で合成したプロピレン重合体（２０ｇ）、及び無水マレイン酸を１０ｇ、ジクミルペルオキシド（DCPO）のトルエン溶液（１０重量％）１２ｇを用い、１１０℃にて反応した以外は、実施例１と同様の操作にて無水マレイン酸変性を行い、該変性重合体を用いて塗装物を作成し、同様に物性評価試験を行った。
【０１０９】
［実施例３］
製造例２で合成したプロピレン重合体を用いた以外は、実施例１と同様の操作にて無水マレイン酸変性を行い、該変性重合体を用いて塗装物を作成し、同様に物性評価試験を行った。
【０１１０】
［実施例４］
製造例３で合成したプロピレン重合体を用いた以外は、実施例１と同様の操作にて無水マレイン酸変性を行い、該変性重合体を用いて塗装物を作成し、同様に物性評価試験を行った。
【０１１１】
［実施例５］
製造例４で合成したプロピレン重合体を用いた以外は、実施例１と同様の操作にて無水マレイン酸変性を行い、該変性重合体を用いて塗装物を作成し、同様に物性評価試験を行った。
【０１１２】
［実施例６］
無水マレイン酸（４ｇ）の代わりにメタクリル酸（５ｇ）を使用し、ジクミルペルオキシド（DCPO）のクロロベンゼン溶液（１０重量％）の添加量を１６ｇから５ｇへ変えた以外は、実施例１と同様の操作にて変性樹脂が得られた。この変性樹脂の赤外線吸収スペクトル測定を行った結果、グラフト量（メタクリル酸基の含量）は、１．１重量％であった。該変性重合体を用いて塗装物を作成し、同様に物性評価試験を行った。
【０１１３】
［実施例７］
無水マレイン酸（４ｇ）の代わりに２−ヒドロキシエチルメタアクリレート（ＨＥＭＡ、５ｇ）を使用し、ジクミルペルオキシド（DCPO）のクロロベンゼン溶液（１０重量％）の添加量を１６ｇから５ｇへ変えた以外は、実施例１と同様の操作にて変性樹脂が得られた。この変性樹脂の赤外線吸収スペクトル測定を行った結果、グラフト量（２−ヒドロキシエチルメタクリレート基の含量）は、１．０重量％であった。該変性重合体を用いて塗装物を作成し、同様に物性評価試験を行った。
【０１１４】
［実施例８］
無水マレイン酸（４ｇ）の代わりに２−ヒドロキシエチルメタアクリレート（ＨＥＭＡ、５ｇ）およびスチレン（Ｓｔ、５ｇ）を使用し、ジクミルペルオキシド（DCPO）のクロロベンゼン溶液（１０重量％）の添加量を１６ｇから５ｇへ変えた以外は、実施例１と同様の操作にて変性樹脂が得られた。この変性樹脂の赤外線吸収スペクトル測定を行った結果、２−ヒドロキシエチルメタアクリレート基の含量は、２．５重量％であった。該変性重合体を用いて塗装物を作成し、同様に物性評価試験を行った。
【０１１５】
［比較例１］
製造例５で合成したプロピレン重合体を用いた以外は、実施例１と同様の操作にて無水マレイン酸変性を行った。変性プロピレン重合体のグラフト量は３．４重量％であり、溶解性試験を行ったところ、トルエンへの溶解性が悪く９６％以上不溶解物が得られ塗装評価ができなかった。但し、ノンタック性は優れていた。その結果を以下の比較例と纏めて表４に示す。
【０１１６】
［比較例２］
製造例６で合成したプロピレン重合体を用いた以外は、実施例１と同様の操作にて無水マレイン酸変性を行った。変性プロピレン重合体のグラフト量は３．５重量％であり、溶解性試験を行ったところ、トルエンへの溶解性は良好であったが、べたつきが多く、塗装評価には至らなかった。またタック性にも問題があった。
【０１１７】
［比較例３］
チーグラー・ナッタ触媒系ポリプロピレン（宇部興産社製ウベタックＵＴ−２１１５）を用い、実施例１と同様の操作にて無水マレイン酸変性を行った。変性プロピレン重合体のグラフト量は３．４重量％であり、トルエンの溶解性試験を行ったところ、不溶解物が２９．５重量％と多く、塗装評価ができなかった。またタック性にも問題があった。
【０１１８】
［比較例４］
プロピレン・ブテン−１共重合体（三井化学社製タフマーＸＲ−１１０Ｔ、プロピレン成分：ブテン−１成分＝７６：２４）を用い、実施例１と同様の操作にて無水マレイン酸変性を行った。変性プロピレン重合体のグラフト量は３．０重量％であり、トルエンの溶解性試験を行ったところ、不溶解物が６７．４重量％と多く、塗装評価ができなかった。但し、ノンタック性は優れていた。
【０１１９】
［比較例５］
変性重合体として、無水マレイン酸変性塩素化ポリプロピレン（Ｅａｓｔｍａｎ社、ＣＰ−３４３−１）を用いて、塗装評価を行った。ノンタック性は優れていたが、特に密着性と耐水性に劣るものであった。
【０１２０】
【表３】
［表３（１）］

【０１２１】
【表４】
［表３（２）］

【０１２２】
【表５】
［表４］

【０１２３】
【発明の効果】
本発明の、ポリプロピレン系塗装成形体は、塗膜密着性に優れ、さらに剛性、耐衝撃性に優れた物性バランスを有する。又、地球環境に有害なハロゲン類を使用していないため、地球環境保護に役立つばかりでなく、ハロゲンの耐候性等への悪影響が大幅に軽減されるため、塗装成形体が長期安定性に優れ、その結果ライフサイクルの延長をもたらし、ひいては限りある地球資源の節約にも貢献する技術開発であるため、その工業的価値は極めて大きい。[0001]
[Field of the Invention]
The present invention relates to a polypropylene-based coated molded body. More specifically, the present invention relates to a polypropylene-based coated molded body obtained by coating a crystalline polypropylene molded body with a coating component containing a polar group-containing propylene-based polymer.
[0002]
[Prior art]
Propylene-based resins such as propylene homopolymer, propylene / ethylene block copolymer composed of propylene homopolymer and propylene / ethylene copolymer are not only lightweight, but also have mechanical properties, moldability, and recycling properties. Therefore, it is used for a wide range of industrial parts. However, since such a propylene-based polymer does not have a so-called polar group, it has a drawback that the coating film adhesion is low at the time of coating for enhancing the design. In order to improve this drawback, the surface of the molded product of the propylene-based polymer is chemically treated with a chemical or the like, or the surface is oxidized using a technique such as corona discharge treatment, plasma treatment, or flame treatment Various approaches have been attempted. However, these methods require not only a special apparatus, but also cannot be said to be sufficient for improving paintability and coating film adhesion.
[0003]
On the other hand, a coating component containing so-called chlorinated polypropylene has been developed as a device for imparting good paintability and coating film adhesion to a propylene polymer by a relatively simple method. Chlorinated polypropylene is generally soluble in organic solvents such as toluene and xylene, and has relatively good adhesion to a propylene polymer as a base material. Therefore, by applying the hydrocarbon solution of the chlorinated polypropylene to the surface of the propylene polymer as a base material and removing the solvent, the paintability and coating film adhesion of the propylene polymer can be improved. It is known to improve. It is known that modified chlorinated polypropylene obtained by further modifying chlorinated polypropylene by graft copolymerization with a polar monomer is further excellent in improving paintability and coating film adhesion.
[0004]
However, since the modified product contains chlorine atoms, there is a problem in terms of the recycling of the resin and generation of harmful substances due to incineration, and its use becomes a social problem in the same way as the vinyl chloride resin. In addition, the chlorine-containing resin still has problems such as inferior weather resistance. Therefore, for chlorinated polypropylene, like vinyl chloride resin, development of an alternative resin containing no halogen such as chlorine is strongly desired. Furthermore, the chlorine-containing resin has problems such as poor weather resistance. Thus, as with vinyl chloride resin, the development of alternative resins that do not contain halogen such as chlorine is strongly demanded for chlorinated polypropylene.
[0005]
On the other hand, as a technique for solving such a problem, a resin containing no chlorine has been developed. For example, Japanese Examined Patent Publication No. 44-958 discloses a treating agent in which an amorphous polypropylene polymer modified with a specific proportion of maleic acid or its anhydride is dissolved in a solvent. Here, the amorphous polypropylene polymer may contain an amorphous polypropylene and a copolymer containing at least about 20 mol% propylene unit and comprising an at least one copolymer monomer and a copolymer of propylene. It is a polymer. Further, as a similar treatment agent, JP-A-8-217835 discloses an amorphous polypropylene or amorphous propylene / 1-butene copolymer obtained by graft copolymerization with an unsaturated carboxylic acid having 3 to 10 carbon atoms. A polymer is disclosed. When such a graft-modified product is used, the solubility is improved and the paintability is excellent compared with general modified propylene-based resins, but the solubility in a solvent at room temperature is still low, stickiness is good, and the coating property is good. It is inferior to film adhesion. For this reason, the chlorinated polypropylene or modified chlorinated polypropylene described above is considered to be relatively excellent as a surface treatment agent and a coating component at present.
[0006]
Therefore, a coated molded body in which chlorinated polypropylene or modified chlorinated polypropylene is applied to a molded body based on a propylene resin has recyclability and environmental problems during incineration, and other amorphous olefin grafts. The coated molded body to which the modified body is applied has problems in terms of quality such as handleability (solubility in a solvent) and stickiness, and a product satisfying the required performance has not been obtained.
[0007]
[Problems to be solved by the invention]
The present invention solves the above-mentioned problems and applies a novel coating component that does not contain a halogen such as chlorine, is not sticky, has excellent solubility in a solvent, and exhibits good coating film adhesion. The present invention provides a polypropylene-based paint molded body.
[0008]
[Means for Solving the Problems]
  The inventors of the present invention have arrived at the present invention as a result of intensive studies to solve the above problems. That is, this invention exists in the polypropylene-type coating molding characterized by coating the base material (B) with the following coating component (A).
Paint component (A): (1), (2) and (3)Has the characteristics ofAnd satisfies the following requirement <1>A coating component comprising a polar group-containing propylene polymer comprising a main chain comprising a propylene polymer and a side chain comprising a carboxyl group, a carboxylic anhydride group or a carboxylic ester group.
(1) Made with a single-site catalyst
(2) When dissolved in heptane at 98 ° C. at a concentration of 10% by weight, the insoluble content is 1% by weight or less.
(3) Having a stereo block structure including both isotactic blocks and amorphous blocks.
<1> Ten types of pentads appearing in a range of 19.8 to 22.2 ppm when the stereoblock structure has a peak top chemical shift of 21.8 ppm attributed to a pentad represented by mmmm. Area S of the peak having 21.8 ppm as the peak top with respect to the total area S of the peaks belonging to ₁ Ratio (S ₁ / S) is 20 to 60%
Base material (B): crystalline polypropylene molded body
[0009]
DETAILED DESCRIPTION OF THE INVENTION
  Hereinafter, the present invention will be described in detail.
<I> Paint component (A)
The polymer constituting the coating component (A) of the present invention is a polar group-containing propylene polymer, and the polymer includes a main chain composed of a propylene polymer having the following characteristics, a carboxyl group, and a carboxylic acid. And a side chain containing an anhydride group or a carboxylic acid ester group (hereinafter collectively referred to as “polar group”).
Hereinafter, a main chain composed of a propylene-based polymer (hereinafter sometimes simply referred to as “main chain”) will be described. The main chain has a number of characteristics, but important characteristics include the following (1)~ (3)And more characteristics(4)~ (7) is added to this.
(1) Made with a single-site catalyst
(2) When dissolved in heptane at 98 ° C. at a concentration of 10% by weight, the insoluble content is 1% by weight or less.
(3) Having a stereo block structure including both isotactic blocks and amorphous blocks.
<1> Ten types of pentads appearing in a range of 19.8 to 22.2 ppm when the stereoblock structure has a peak top chemical shift of 21.8 ppm attributed to a pentad represented by mmmm. Area S of the peak having 21.8 ppm as the peak top with respect to the total area S of the peaks belonging to ₁ Ratio (S ₁ / S) is 20 to 60%
[0010]
Characteristics (1) Manufactured by single site catalyst
The main chain of the polar group-containing propylene polymer contained in the coating component (A) is obtained by a method of polymerizing with a single site catalyst. Single-site catalysts are characterized by the ability to control microtacticity through ligand design, the ability to easily produce polymers with relatively low molecular weight, and the sharp molecular weight distribution and stereoregularity distribution of polymers. As mentioned. If the molecular weight distribution or the stereoregular distribution is irregular, the solubility may be different, and a partially insoluble one may be formed.
Among single-site catalysts, metallocene catalysts are preferably used in that the microtacticity can be precisely controlled. As shown below, the metallocene-based catalyst includes a metallocene compound ([a] component) and a cocatalyst ([b] component) as essential components.
[0011]
As the metallocene compound ([a] component), C having a transition metal-containing crosslinking group₁Symmetric ansa-metallocene is preferred. Non-crosslinked metallocene is also applicable to the production of the propylene-based polymer of the present invention. In general, an ansa-metallocene having a crosslinking group is preferable from an industrial standpoint because it is superior in thermal stability and the like. .
The ansa-metallocene having a transition group containing a transition metal used in the present invention is a C of a bridged Group 4 transition metal compound having a conjugated 5-membered ring ligand.₁-Metallocene with symmetry. Such a transition metal compound is known and it is also known to use it as a catalyst component for α-olefin polymerization.
[0012]
The metallocene compound of component [a] is represented by the following general formula (1) and C₁-A compound having symmetry. A plurality of metallocene compounds represented by the general formula may be mixed and used.
Q (C_FiveH_4-aR² _a) (C_FiveH_4-bR^Three _bMXY (1)
In the general formula (1), Q is a bonding group that bridges two conjugated 5-membered ring ligands, M is a group 4 transition metal of the periodic table, X and Y are each independently hydrogen, halogen, C1-C20 hydrocarbon group, C1-C20 oxygen-containing hydrocarbon group, C1-C20 nitrogen-containing hydrocarbon group, C1-C20 phosphorus-containing hydrocarbon group, or C1-C1 20 silicon-containing hydrocarbon groups are R²And R^ThreeAre each independently a hydrocarbon group having 1 to 20 carbon atoms, halogen, a halogen-containing hydrocarbon group having 1 to 20 carbon atoms, an alkoxy group, an aryloxy group, a silicon-containing hydrocarbon group, a phosphorus-containing hydrocarbon group, nitrogen A hydrocarbon-containing group or a boron-containing hydrocarbon group. Two adjacent Rs²And / or R^ThreeMay be bonded to each other to form a 4- to 10-membered ring. a and b are each independently an integer satisfying 0 ≦ a ≦ 4 and 0 ≦ b ≦ 4.
[0013]
Of the metallocene compounds represented by the general formula (1), dichloro [dimethylsilylene (cyclopentadienyl) (2,4-dimethyl-4H-1-azulenyl)] hafnium is most preferable, and dichloro [dimethyl Germylene (cyclopentadienyl) (2,4-dimethyl-4H-1-azurenyl)] hafnium or dichloro [dimethylsilylene (2-methyl-1-indenyl) (2,4-dimethyl-4H-1-azurenyl) Hafnium is also a suitable catalyst.
[0014]
In addition, as a metallocene compound, the mixture of the compound which has several different structures may be used, and may be used in combination of 2 or more types. Further, a known solid catalyst mainly composed of titanium trichloride and a carrier-supported catalyst containing magnesium, titanium, and halogen as essential components can be used supplementarily. Further, the [a] component may be newly added at the end of the first stage of polymerization or before the start of polymerization in the second stage.
[0015]
In the present invention, the cocatalyst used as the component [b] includes (1) an organoaluminum oxy compound as an essential component and (2) a reaction with a transition metal of the component [a] to convert the component [a] into a cation. One or more substances selected from the group consisting of (3) Lewis acid, (4) ion-exchangeable layered compound excluding silicate, or inorganic silicate are used.
[0016]
In the production of the main chain of the propylene polymer of the present invention, an organoaluminum compound may be used as the optional component [c] in addition to the cocatalyst [b] component. Specifically, it is a trialkylaluminum, a halogen- or alkoxy-containing alkylaluminum, or a hydrogen-containing organoaluminum compound. Of these, trialkylaluminum such as trimethylaluminum, triethylaluminum, tripropylaluminum, and triisobutylaluminum is particularly preferable. Two or more of these optional components may be used in combination. Further, an optional component [c] may be newly added after the start of polymerization.
[0017]
The metallocene catalyst can be obtained by contacting the [a] component, the [b] component, and the optional [c] component, but the contacting method is not particularly limited. This contact may be performed not only at the time of catalyst preparation but also at the time of prepolymerization or polymerization of propylene.
A solid of an inorganic oxide such as a propylene polymer, silica, alumina, or the like may be allowed to coexist or contact when the catalyst components are contacted or after contact.
The contact may be performed in an inert gas such as nitrogen, or may be performed in an inert hydrocarbon solvent such as n-pentane, n-hexane, n-heptane, toluene and xylene. These solvents are preferably used after an operation for removing poisoning substances such as water and sulfur compounds. The contact temperature is between −20 ° C. and the boiling point of the solvent used, and particularly preferably between room temperature and the boiling point of the solvent used.
[0018]
Although there is no restriction | limiting in particular in the usage-amount of each catalyst component, When using the ion exchange layered compound except a silicate, or an inorganic silicate as a [b] component, [a] component per 1g of [b] component Is 0.0001 to 10 mmol, preferably 0.001 to 5 mmol, and the [c] component is 0 to 10,000 mmol, preferably 0.01 to 100 mmol. In addition, the atomic ratio of the transition metal in the [a] component to the aluminum in the [c] component is controlled to be 1: 0 to 1,000,000, preferably 1: 0.1 to 100,000. Is preferable in terms of polymerization activity.
The catalyst thus obtained may be used after washing with an inert hydrocarbon solvent such as n-pentane, n-hexane, n-heptane, toluene, xylene or the like, or may be used without washing. Good.
When washing, a new [c] component may be used in combination as necessary. The amount of the [c] component used at this time is preferably 1: 0 to 10,000 in terms of the atomic ratio of aluminum in the [c] component to the transition metal in the [a] component.
[0019]
As the catalyst, it is also possible to use a polymer obtained by preliminarily polymerizing propylene and washing it as necessary. This prepolymerization may be carried out in an inert gas such as nitrogen or in an inert hydrocarbon solvent such as pentane, hexane, heptane, toluene, xylene.
The polymerization reaction of propylene is performed in the presence or absence of an inert hydrocarbon such as propane, n-butane, n-hexane, n-heptane, toluene, xylene, cyclohexane, methylcyclohexane, or a liquid of liquefied propylene. Of these, the polymerization is preferably performed in the presence of the above-described inert hydrocarbon.
[0020]
Specifically, the propylene polymer is produced in the presence of the [a] component and the [b] component, or the [a] component, the [b] component, and the [c] component. The polymerization temperature, polymerization pressure, and polymerization time are not particularly limited, but usually optimum settings can be made in consideration of productivity and process capability from the following ranges. That is, the polymerization temperature is usually 0 to 150 ° C., preferably 20 to 100 ° C., the polymerization pressure is 0.1 to 100 MPa, preferably 0.3 to 10 MPa, more preferably 0.5 to 4 MPa, and the polymerization time. Is selected from the range of 0.1 to 10 hours, preferably 0.3 to 7 hours, more preferably 0.5 to 6 hours.
[0021]
The main chain made of a propylene polymer is a homopolymer having propylene as a monomer or a copolymer having propylene as a main component. The propylene homopolymer means a polymer having a propylene content of substantially 100% by weight. A copolymer containing propylene as a main component is one containing a small amount of another monomer as a copolymerization component. In the present invention, the propylene content is usually 95% by weight or more, preferably 99.5% by weight or more, and more preferably 99.9% by weight or more. When the propylene content is less than 95% by weight, it is difficult for the isotactic block to grow, and a tendency that the adhesion of the coating film to the substrate is lowered is observed. The propylene copolymer is characterized by increased solubility in solvents such as heptane and toluene as compared to a homopolymer.
[0022]
Examples of the copolymer component include monomers having an olefinic double bond, such as ethylene, butene, pentene, hexene, octene, decene, butadiene, hexadiene, octadiene, cyclobutene, cyclopentene, cyclohexene, norbornene, norbornadiene, styrene, and these. A suitable one can be selected from the derivatives. Of these, ethylene, butene, pentene, hexene and octene are preferred, and ethylene and butene are more preferred.
[0023]
Characteristic (2) When dissolved in heptane at 98 ° C. at a concentration of 10% by weight, the insoluble content is 1% by weight or less.
The propylene polymer main chain produced using the single-site catalyst described in the characteristic (1) is very superior in solubility compared to normal highly stereoregular isotactic polypropylene, and it has a boiling heptane ( When dissolved in a concentration of 10% by weight at 98 ° C., the insoluble component is 1% by weight or less of the total amount of the polymer. Preferably it is 0.1 weight% or less, More preferably, it is a state without an insoluble component. When the insoluble component exceeds 1% by weight, the solubility is insufficient, so that the coating performance such as rough skin and smoothness of the coating film tends to be lowered, and the workability in the coating process tends to be lowered.
As a measuring method, for example, a solution dissolved at a predetermined temperature and a predetermined concentration is filtered around the temperature (filtered when hot if the temperature is high), and the filter paper or SUS wire mesh (weight in advance) is used. The method of measuring the weight of insoluble matter is used.
[0024]
Characteristic (3) Having a stereo block structure including both isotactic block and amorphous block
The main chain composed of a propylene-based polymer is one having a small amount of insoluble heptane produced by a specific catalyst as represented by (1) and (2) as described above. Above all,¹³What has the characteristic (3) prescribed | regulated by a C-NMR spectrum is preferable. This characteristic (3) is a structure in which a highly crystalline block and a highly amorphous block coexist in a well-balanced manner in the main chain of the propylene polymer, and the highly crystalline block is rich in isotacticity. Represents that In other words, if there are too many highly crystalline blocks in the polymer, the solubility in the solvent will deteriorate, so the balance between the highly crystalline block and the highly amorphous block is important. As part¹³The requirements defined by the C-NMR spectrum apply.
[0025]
In the present invention¹³The measuring method of C-NMR spectrum is as follows.
350-500 mg of sample is completely dissolved in about 10 ml of NMR sample tube using about 2.2 ml of orthodichlorobenzene. Next, about 0.2 ml of deuterated benzene is added as a lock solvent and homogenized, and then measurement is performed at 130 ° C. by a proton complete decoupling method. Measurement conditions are flip angle 90 °, pulse interval 5T.₁(T₁Is the longest value of the spin-lattice relaxation time of the methyl group. In the propylene-based polymer, since the spin-lattice relaxation time of the methylene group and the methine group is shorter than that of the methyl group, the recovery of the magnetization of all the carbons is 99% or more under this measurement condition. In order to improve the quantitative accuracy,¹³It is preferable to perform integration for 20 hours or more using an NMR apparatus having a resonance frequency of C nucleus of 125 MHz or more.
[0026]
The chemical shift is a methyl branch of 10 types of pentads (mmmm, mmmr, rmrr, mmrr, mmrm, rmrr, rmrm, rrrr, rrrr, mrrm) of propylene unit linkages composed of head-to-tail bonds. The absolute chemical configuration of all is the same, that is, the chemical shift of the peak based on the methyl group of the third unit of 5 units of propylene units expressed in mmmm is set as 21.8 ppm, and other carbon peaks are based on this. Determine the chemical shift. In this standard, for example, in the case of other five propylene units, the chemical shift of the peak based on the methyl group of the third unit is generally as follows.

The chemical shift of the peak derived from these pentads varies slightly depending on the NMR measurement conditions, and the peak is not necessarily a single peak, but a complex splitting pattern based on a fine structure ( It should be noted that the split pattern) is often shown. In the present invention, the isotactic block refers to a mmmm pentad, and the amorphous block refers to all other pentads including at least one r dyad.
[0027]
  In the present invention, the important feature of the stereo block structure is the following requirements:<1> and <2>It is.
<1>  With respect to the total area S of the peaks belonging to the above 10 types of pentads appearing in the range of 19.8 to 22.2 ppm when the peak top chemical shift of the peak represented by mmmm is 21.8 ppm. Peak area S with 21.8 ppm peak top₁Ratio (S₁/ S)20~ 60%
<2>  The area of a peak (mmmr) having a peak top at 21.5 to 21.7 ppm is defined as S₂When S₁And S₂The relationship is 4 + 2S₁/ S₂Satisfy> 5.
[0028]
S against S₁If the ratio is less than 10%, the crystallinity is too low, sufficient coating film adhesion cannot be obtained, and problems such as stickiness are liable to occur. On the other hand, S against S₁If the ratio exceeds 60%, on the contrary, the crystallinity is too high and the solubility in a solvent is lowered, which is also not preferable. S against S₁The ratio is preferably 20 to 50%, more preferably 30 to 50%.
[0029]
  S₁And S₂The above requirements<2>Examples of the method of controlling to be within the range specified in (i) include (i) a method of controlling by the structure of the polymerization catalyst, (ii) a method of controlling by the polymerization temperature, (iii) a method of controlling by the monomer concentration; Can do. S₁, S₂The temperature dependency and the monomer concentration dependency depend on the catalyst used, and cannot be generally stated. Therefore, it is important to control these conditions based on the nature of the catalyst used. Moreover, when controlling by the structure of a polymerization catalyst, the structure of the ligand which comprises a transition metal component is important. In particular, when a bridged metallocene is used, a substituent at the α-position with respect to the bridgehead of the bridge group is important. In general, stereoselectivity is likely to improve when there is a substituent that is somewhat bulky at the α-position. Furthermore, when a bridged metallocene containing a ligand having a condensed ring such as an indenyl group or an azulenyl group is used, the structure of the 4-position substituent also greatly affects the stereoselectivity. In general, stereoselectivity is likely to improve when there is a somewhat bulky substituent at the 4-position. Conversely, by introducing a sterically small substituent at the 4-position, it is possible to effectively reduce the stereoselectivity and reduce the crystallinity of the resulting polymer.
[0030]
  Further, as a feature of the stereo block structure of the present invention, the following requirements<3> to <10>Is mentioned. All of these requirements are such that a highly crystalline block and a highly amorphous block coexist in the main chain of the propylene polymer, and the highly crystalline block is rich in isotacticity. Is closely related to being.
<3>  The area of the peak (rrrr) having a peak top at 20.3 to 20.5 ppm is defined as S_ThreeThe area S_ThreeRatio (S_Three/ S) is 0.2 to 3%
<4>  The area of a peak (rmrm) having a peak top at 20.6 to 20.8 ppm is defined as S_FourThe area S_FourRatio (S_Four/ S) is 0.3-7%
<5>  S_FourIs S_ThreeBigger than,
<6>  S₁And S₂The relationship is 25> 4 + 2S₁/ S₂> 5
<7>  Area S₁Ratio (S₁/ S) is 30-50%
<8>  Area S_ThreeRatio (S_Three/ S) is 1 to 3%
<9>  Area S_FourRatio (S_Four/ S) is 4-7%,
<10>S₁And S₂The relationship is 10> 4 + 2S₁/ S₂> 7
[0031]
  Propylene polymer main chain is a requirement<2>Like 4 + 2S₁/ S₂It is preferable to satisfy the relationship> 5. This relational expression is closely related to an index named as isotactic block index (BI) by Waymouth et al. BI is an index representing the stereoblock property of the polymer, and is defined by BI = 4 + 2 [mmmm] / [mmmr]. More specifically, BI represents the average chain length of isotactic blocks having 4 or more propylene units (JW Collette et al., Macromol., 22, 3858 (1989); Randall, J. Polym. Sci. Polym. Phys. Ed., 14, 2083 (1976)). For statistically perfect atactic polypropylene, BI = 5. Therefore, BI = 4 + 2 [mmmm] / [mmmr]> 5 means that the average chain length of isotactic blocks contained in the polymer is longer than that of atactic polypropylene.
[0032]
  Requirement<2>, <6> or <10>4 + 2S₁/ S₂Is not exactly the same as the above-mentioned BI, but is roughly compatible with 4 + 2S₁/ S₂> 5 requirement<2>Means that, unlike atactic polypropylene, the polymer main chain of the present invention contains an isotactic block having a crystallizable chain length. The presence of an atactic block means that, in other words, a block composed of a sequence having a disordered stereospecificity is also present in the main chain. In this way, a crystalline block and an amorphous block coexist in the main chain, and the crystalline block is formed from an isotactic block having a relatively long average chain length, It is a unique structure that has a structure rich in tacticity.
[0033]
Characteristic (4) When dissolved at a concentration of 10% by weight in toluene at 25 ° C., the insoluble content is 1% by weight or less.
When it is dissolved at a concentration of 10% by weight in toluene (25 ° C.) at room temperature, those exhibiting the same level of solubility as the characteristic (2) are preferable.
As a measuring method, for example, a solution dissolved at a predetermined temperature and a predetermined concentration is filtered around the temperature (filtered when hot if the temperature is high), and the filter paper or SUS wire mesh (weight in advance) is used. The method of measuring the weight of insoluble matter is used.
When the toluene insoluble content exceeds 1% by weight, the solubility is insufficient, and thus the coating performance such as rough skin and smoothness of the coating film tends to deteriorate, and the storage stability in the solution state when used as a coating material. Is unfavorable because it tends to be deteriorated and easily separated and the workability in the coating process is reduced.
[0034]
Property (5) The weight average molecular weight Mw measured by GPC is 5,000 to 1,000,000.
The weight average molecular weight Mw measured by GPC (Gel Permeation Chromatography) is preferably 5,000 to 1,000,000. When Mw is less than 5,000, not only the film-forming property after coating on a substrate using a polar group-containing propylene polymer modified by graft copolymerization is deteriorated, but also stickiness is not preferable. . When Mw exceeds 1,000,000, there is no significant problem with respect to film-forming properties and tackiness, but the viscosity when the polar group-containing propylene polymer is dissolved in a solvent becomes too high, resulting in production or the polarity. This is not preferable because it causes inconvenience in handling the group-containing propylene polymer solution. In the present invention, the preferred weight average molecular weight Mw is in the range of 5,000 to 1,000,000, more preferably 10,000 to 500,000, and still more preferably 30,000 to 200,000.
[0035]
A conventionally known method can be used to adjust the molecular weight of the polymer. That is, a method of controlling the molecular weight by controlling the polymerization temperature, a method of controlling the molecular weight by controlling the monomer concentration, and a method of controlling the molecular weight by using a chain transfer agent. Hydrogen is preferred when a chain transfer agent is used.
The molecular weight measurement by GPC can be performed by a conventionally known method using a commercially available apparatus using orthodichlorobenzene as a solvent and polystyrene as a standard sample.
The molecular weight distribution is not particularly limited, but an excessively broad molecular weight distribution should be avoided because it means that the content of low molecular weight components is inevitably high. When the ratio Mw / Mn between the weight average molecular weight Mw and the number average molecular weight Mn is used as an index of the molecular weight distribution, preferably Mw / Mn <20, more preferably Mw / Mn <10, most preferably Mw / Mn <5. Are preferably used.
[0036]
Characteristic (6) There is no clear peak corresponding to a heat of crystal melting measured by DSC of 1 J / g or more.
In the propylene polymer main chain, the presence of a clear peak corresponding to a heat of crystal fusion of 1 J / g is not preferable because the solubility in a solvent is lowered. As a measurement method, using a thermal analysis system (DSC), the sample is melted at 200 ° C. for 3 minutes, then the temperature is lowered to 30 ° C. at a rate of 10 ° C./minute, and the temperature is raised to 200 ° C. at 10 ° C./minute. To obtain a melting curve. It is evaluated from the melting curve in the last temperature rising stage whether a clear peak corresponding to 1 J / g or more exists in the temperature range of 50 to 160 ° C. When there was a peak, the peak top temperature was taken as the melting point, and the heat of crystal fusion was determined from the endothermic peak area.
[0037]
Characteristic (7) Dissolve substantially all in ortho-dichlorobenzene (ODC) at 60 ° C.
As described in the characteristic (3), the propylene-based polymer main chain has an appropriate stereoregular distribution of methyl groups, and therefore has a relatively low crystallinity and excellent solubility in a solvent. Specifically, when the polymer is fractionated at elevated temperature with orthodichlorobenzene (ODC), substantially all components are eluted at 60 ° C. or lower. The component that elutes at a temperature higher than 60 ° C. is a component having a considerably high crystallinity. Therefore, when the polymer contains such a component, such a crystal is dissolved when the polymer is dissolved in a solvent. Inconveniences such as highly soluble components becoming insoluble components and gelation tend to occur. It is preferable that substantially all components elute preferably at 50 ° C. or lower, more preferably at 40 ° C. or lower.
[0038]
As described in the characteristics (2), (4), and (7), the propylene polymer main chain is excellent in solubility in an organic solvent. Examples of organic solvents other than heptane, toluene, and orthodichlorobenzene include aromatic hydrocarbons such as benzene and xylene; aliphatic hydrocarbons such as n-pentane, n-hexane, n-octane, and n-decane; cyclohexane, Alicyclic aliphatic hydrocarbons such as methylcyclohexane and dimethylcyclohexane, halogenated hydrocarbons such as methylene chloride, carbon tetrachloride, trichloroethylene, perchlorethylene and chlorobenzene, esters such as n-ethyl acetate and n-butyl acetate , Ketones such as methyl isobutyl ketone and cyclohexanone, and polar solvents such as tetrahydrofuran and dimethyl sulfoxide. Among these, aromatic hydrocarbons or halogenated hydrocarbons are preferable, and toluene, xylene, and chlorobenzene are particularly preferable.
These organic solvents are suitably used as a solvent for the modification reaction of the propylene polymer main chain or a coating vehicle for dissolving the modification reaction product.
[0039]
Next, the polar group of the polar group-containing propylene polymer will be described. In the present invention, the “polar group” is a general term for a carboxyl group, a carboxylic anhydride group or a carboxylic ester group, and corresponds to a side chain of a polar group-containing propylene polymer.
As a method for introducing a polar group into the propylene polymer main chain, a method of graft copolymerizing a polymerizable monomer containing a carboxyl group or the like is common.
[0040]
Examples of the polymerizable monomer containing a carboxyl group to be graft copolymerized include (meth) acrylic acid and acid derivatives thereof, and monoolefin dicarboxylic acid, anhydrides and monoesters thereof, and at least one selected from these. A seed is used. Specifically, (meth) acrylic acid and its ester derivatives include (meth) acrylic acid; (meth) acrylic acid ester monomers having an alkyl group having 1 to 12 carbon atoms, such as (meth) acrylic acid Methyl, ethyl (meth) acrylate, n-propyl (meth) acrylate, isopropyl (meth) acrylate, n-butyl (meth) acrylate, isobutyl (meth) acrylate, t-butyl (meth) acrylate, Pentyl (meth) acrylate, hexyl (meth) acrylate, cyclohexyl (meth) acrylate, octyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, nonyl (meth) acrylate, decyl (meth) acrylate , Dodecyl (meth) acrylate, etc .; aryl group or arylalkyl group having 6 to 12 carbon atoms A (meth) monomers acrylic acid ester, for example (meth) acrylate, phenyl (meth) toluyl acrylate include benzyl (meth) acrylate and the like.
[0041]
Furthermore, as other (meth) acrylic acid derivatives, monomers of (meth) acrylic acid esters having a C1-C20 alkyl group containing a hetero atom, such as hydroxyethyl (meth) acrylate, (meth) acrylic acid Dimethylaminoethyl, diethylaminoethyl (meth) acrylate, (meth) acrylic acid-2-aminoethyl, (meth) acrylic acid-2-methoxyethyl, (meth) acrylic acid-3-methoxypropyl, (meth) acrylic acid Glycidyl, adducts of (meth) acrylic acid ethylene oxide, etc .; (meth) acrylic acid ester monomers having a fluorine atom-containing alkyl group having 1 to 20 carbon atoms, such as trifluoromethyl methyl (meth) acrylate, ( (Meth) acrylic acid-2-trifluoromethylethyl, (meth) acrylic acid- - perfluoro ethyl ethyl, and the like; (meth) acrylamide monomers such as (meth) acrylamide, (meth) acrylic dimethyl amides.
[0042]
Examples of the monoolefin dicarboxylic acid include maleic acid, chloromaleic acid, citraconic acid, itaconic acid, glutaconic acid, 3-methyl-2-pentene diacid (3-methyl-2-pentene-1,5-dicarboxylic acid ), 2-methyl-2-pentene / diacid, 2-hexene / dioic acid, and the like. Examples of monoolefin dicarboxylic acid monoalkyl esters include monoesters of alkyl alcohols having 1 to 12 carbon atoms and these dicarboxylic acids. Examples of alkyl alcohols include methyl alcohol, ethyl alcohol, and propyl alcohol. Butyl alcohol, pentyl alcohol, octyl alcohol, cyclohexyl alcohol and the like.
[0043]
When a coating film is formed using the polar group-containing propylene-based polymer of the present invention, from the viewpoint of coating film adhesion between the coating film and the substrate, polymerizable monomers containing these grafted carboxyl groups and the like The solubility parameter is preferably higher, that is, an unsaturated carboxylic acid derivative component composed of an unsaturated carboxylic acid having 3 to 10 carbon atoms, an acid anhydride and an ester thereof is preferable. Maleic anhydride is particularly preferable.
[0044]
Among the polar group-containing propylene-based polymers used in the present invention, a modified polymer having a monoolefin dicarboxylic acid monoalkyl ester as a graft copolymer unit is, for example, a graft copolymer of a monoolefin dicarboxylic acid monoalkyl ester to a polymer. Polymerization method: A monoolefin dicarboxylic acid or its anhydride can be obtained by graft copolymerization with a propylene-based polymer and then esterifying one of the carboxylic acid groups with an alkyl alcohol.
[0045]
The graft amount of at least one graft copolymerized unit selected from polymerizable monomers containing a carboxyl group or the like in the polar group-containing propylene polymer, that is, the content in the modified polymer is used as a primer in the molded product. When applied, a coating film with high adhesion of the paint is obtained, and the adhesion between the coating film and the molded product is good and the appearance is good. Graft copolymerize to ˜15 wt%.
[0046]
Various known methods may be used as a method of graft copolymerizing a polymerizable monomer such as monoolefin dicarboxylic acid, its anhydride, and monoolefin dicarboxylic acid monoalkyl ester with the propylene-based polymer. For example, a method of conducting a graft copolymerization reaction by dissolving a propylene polymer in an organic solvent, adding the above-mentioned grafting polymerizable monomer and radical polymerization initiator and stirring under heating; heating the propylene polymer; Graft copolymerization by adding a polymerizable monomer and a radical polymerization initiator which are dissolved and grafted to the melt and stirring; or graft copolymerization while heating and kneading each component to an extruder A method of impregnating a propylene-based polymer powder with a solution obtained by dissolving the polymerizable monomer to be grafted and a radical polymerization initiator in an organic solvent, and then heating to a temperature at which the powder does not dissolve and graft copolymerizing. Etc.
[0047]
At this time, the ratio of radical polymerization initiator / polymerizable monomer to be grafted is usually in the range of 1/100 to 3/5, preferably 1/20 to 1/2 in terms of molar ratio. The reaction temperature is preferably 50 ° C. or higher, particularly 80 to 200 ° C., and the reaction time is about 2 to 10 hours.
[0048]
The radical polymerization initiator used for the graft copolymerization can be appropriately selected from ordinary radical initiators, and examples thereof include organic peroxides and azonitriles. Organic peroxides include diisopropyl peroxide, di (t-butyl) peroxide, t-butyl hydroperoxide, benzoyl peroxide, dicumyl peroxide, cumyl hydroperoxide, dilauroyl peroxide, dibenzoyl peroxide Methyl ethyl ketone peroxide, cyclohexanone peroxide, cumene hydroperoxide, diisopropyl peroxycarbonate, dicyclohexyl peroxycarbonate and the like. Examples of the azonitrile include azobisbutyronitrile and azobisisopropylnitrile. Of these, benzoyl peroxide and dicumyl peroxide are preferred.
[0049]
When the graft copolymerization reaction is carried out using an organic solvent, specific examples of the organic solvent include aromatic hydrocarbons such as benzene, toluene and xylene; aliphatic systems such as hexane, heptane, octane and decane. Hydrocarbons: Halogenated hydrocarbons such as trichloroethylene, perchlorethylene, chlorobenzene, o-dichlorobenzene, etc., and among these, aromatic hydrocarbons or halogenated hydrocarbons are preferred, particularly toluene, xylene, chlorobenzene. Is preferred.
[0050]
  The modified propylene polymer of the present invention can also be dissolved in the same solvent as the above-mentioned solvent in which the propylene polymer before modification is soluble. The modified propylene polymer of the present invention has a solubility parameter of 11 (cal / cm) among solvents.^Three)^1/2Since the solubility in the following solvents is high, the graft-modified product of this propylene polymer has a solubility parameter of 11 (cal / cm^Three)^1/2In the following solvents1% by weightThe dissolved composition is effective as a coating composition.
[0051]
Solubility parameter is 11 (cal / cm^Three)^1/2Specific examples of the following solvents include aromatic hydrocarbons such as benzene, toluene and xylene; aliphatic hydrocarbons such as n-pentane, n-hexane, n-heptane, n-octane and n-decane; cyclohexane Cycloaliphatic hydrocarbons such as methylcyclohexane and dimethylcyclohexane, halogenated hydrocarbons such as methylene chloride, chloroform, carbon tetrachloride, trichloroethylene, perchlorethylene, chlorobenzene, o-dichlorobenzene, n-methyl acetate, Examples include esters such as n-ethyl acetate and n-butyl acetate, ketones such as methyl isobutyl ketone and cyclohexanone, ethers such as tetrahydrofuran, etc. Among these, aromatic hydrocarbons or halogenated hydrocarbons are preferable, Especially toluene, xylene, Rorubenzen is preferable.
[0052]
The coating composition of the present invention is mainly composed of a coating component (A) and an organic solvent that dissolves the coating component (A), and various kinds of antioxidants, weathering stabilizers, heat resistance inhibitors, etc., if necessary. Stabilizer: It may contain a colorant such as titanium oxide or an organic pigment, or a conductivity imparting agent such as carbon black or ferrite.
[0053]
Since the polar group-containing propylene polymer of the present invention is soluble in a solvent as described above, it can be applied to a molded body of an olefin polymer having crystallinity. Of these olefin polymers, propylene polymers are preferably used. Also, molded products made of polypropylene and synthetic rubber, molded products made of polyamide resin, unsaturated polyester resin, polybutylene terephthalate resin, polycarbonate resin, etc., such as molded products such as automobile bumpers, and further for steel plate and electrodeposition treatment It can also be used for surface treatment of steel plates and the like. In addition, the surface is coated with paint, primer, adhesive, etc. mainly composed of polyurethane resin, fatty acid-modified polyester resin, oil-free polyester resin, melamine resin, epoxy resin, etc., and adherence of paint, etc. to the surface Can be used to form a coating film that is excellent in sharpness and low-temperature impact properties.
[0054]
Since the coating film formed when the coating component (A) containing the polar group-containing propylene-based polymer of the present invention is applied to the base material (B) exhibits good adhesion to the base material, It can be used as a coating film adhesive resin for a material. In addition, in order to acquire favorable adhesiveness with respect to a base material, it is preferable to heat after application | coating. Although there is no restriction | limiting in particular in heating temperature, Considering practicality, it is preferable to set it as 50-150 degreeC, Furthermore, it is 60-130 degreeC. There is no restriction | limiting in particular also in the method of application | coating, A conventionally well-known method, such as the method of apply | coating with a spray, the method of apply | coating with a roller, the method of applying with a brush, can be used.
[0055]
The coating component (A) containing the polar group-containing propylene polymer of the present invention is applied, and the coating is formed on the surface of the molded product by a method such as electrostatic coating, spray coating, brush coating, or the like. Can be applied.
The coating may be applied by a method of overcoating after undercoating. After applying the coating material, the coating film is cured according to a normal method of heating by electric heating, infrared rays, high frequency, etc., and a molded product having a desired coating film on the surface can be obtained. The method for curing the coating film is appropriately selected depending on the material and shape of the molded product, the properties of the paint used, and the like.
[0056]
The coating component (A) containing a polar group-containing propylene polymer can be used as a primer component. That is, it can be applied to the surface of the substrate (B) and used as a primer component for improving coating film performance such as adhesion of paint to the surface, water resistance and gasoline resistance.
Specifically, an acrylic resin and / or a polyester resin and a polyurethane-modified polypropylene resin and the polar group-containing propylene polymer can be applied to the base material (B). Such a primer does not contain a halogen such as chlorine, is not sticky, has excellent solubility, is excellent in compatibility with acrylic resins and polyester resins, has good adhesion to the substrate, and is coated. Thus, it becomes possible to form a coating film having high water resistance and gasohol resistance.
[0057]
The coating component (A) containing a polar group-containing propylene polymer can be used as a base color component that does not require application of a primer component. That is, when applying to the surface of the base material (B), it does not require surface treatment or cleaning of the base material, primer application is unnecessary, and a coating film having good water resistance and weather resistance is formed by a single coating. It can be used as a possible base color component.
[0058]
Such a base color does not contain a halogen such as chlorine, is not sticky, has excellent solubility, is excellent in compatibility with acrylic polyol and polyester polyol, and is a crystalline propylene polymer as a base material It is possible to form a coating film with high durability and chemical resistance, maintaining good adhesion and coating properties to polyolefins such as A coating film having water resistance and weather resistance can be formed.
[0059]
It is also possible to further improve the adhesion of the coating film by applying a primer component to the substrate.
[0060]
<II> Substrate (B) component
The base material (B) used in the present invention is a molded body of crystalline polypropylene. Here, the crystalline polypropylene is a molded product made of a propylene homopolymer and / or a propylene / ethylene block copolymer comprising a propylene homopolymer part and a propylene / ethylene copolymer part.
[0061]
The MFR of the propylene homopolymer and the propylene / ethylene block copolymer is preferably 2 g / 10 min or more, more preferably 10 to 300 g / 10 min, and particularly preferably 25 to 200 g / 10 min.
When the MFR of the propylene / ethylene block copolymer and the propylene homopolymer is less than 2 g / 10 minutes, the flowability tends to be insufficient. On the contrary, if it is extremely high, the mechanical properties are inferior.
The MFR of the propylene / ethylene block copolymer may be adjusted at the time of polymerization or adjusted with an organic peroxide such as diacyl peroxide or dialkyl peroxide after the polymerization.
[0062]
The propylene / ethylene block copolymer is a propylene / ethylene block copolymer containing a crystalline polypropylene part (a unit part) and an ethylene / propylene random copolymer part (b unit part).
The a unit is usually obtained by homopolymerization of propylene, and in some cases, by copolymerizing propylene with a small amount of other α-olefin.
The MFR of the polypropylene homopolymer of a unit part is preferably 10 g / 10 min or more, more preferably 15 to 500 g / 10 min, still more preferably 20 to 400 g / 10, particularly preferably 40 to 300 g / 10. Minutes.
When the MFR of the propylene homopolymer part (a unit part) of the propylene / ethylene block copolymer is less than 10 g / 10 minutes, the flowability tends to be insufficient. Conversely, when the MFR is extremely high, the mechanical properties tend to be inferior.
[0063]
On the other hand, the b unit is a rubbery component obtained by random copolymerization of propylene and ethylene.
The propylene content of the propylene / ethylene copolymer part (b unit part) is preferably 30 to 85% by weight, more preferably 40 to 80% by weight, and still more preferably 50 to 75% by weight. When the propylene content of the copolymer part departs from the above range, the dispersibility tends to deteriorate and the glass transition temperature tends to increase, and the impact characteristics tend to deteriorate.
The propylene content of the propylene / ethylene copolymer part can be adjusted by controlling the concentration ratio of propylene and ethylene during the polymerization of the propylene / ethylene copolymer part.
[0064]
The molecular weight of the propylene / ethylene copolymer part is not particularly limited, but in consideration of dispersibility and impact resistance, the weight average molecular weight (Mw) is preferably 200,000 to 3,000,000, more preferably It is 300,000-2,500,000, More preferably, it is 400,000-2 million.
[0065]
Although there is no restriction | limiting in particular about the quantity of a unit part and b unit part, Generally a unit part becomes like this. Preferably it is 95 weight% or less of total polymerization amount, More preferably, it is 50-95 weight%, More preferably, it is 60-90 weight % And b unit parts are preferably adjusted to be 5% by weight or more of the total polymerization amount, more preferably 5 to 50% by weight, and still more preferably 10 to 40% by weight.
If the amount of the b unit part is less than the above range, the impact resistance expected as a block copolymer tends to be insufficient, and if it exceeds the above range, rigidity, strength and heat resistance tend to be insufficient. There is not preferable.
[0066]
In this invention, the quantity of this copolymer part shall be measured using a temperature rising elution fractionation method. That is, the a unit part does not elute at 100 ° C. or lower in the extraction with orthodichlorobenzene, but the b unit part elutes easily. Therefore, the composition of the propylene / ethylene block copolymer is determined by extraction analysis with the above-described orthodichlorobenzene for the polymer after production.
The amount of the propylene / ethylene copolymer portion can be adjusted by controlling the ratio of the polymerization amount of the propylene homopolymer portion and the polymerization amount of the propylene / ethylene copolymer portion by the polymerization time or the like.
[0067]
The production method of the propylene homopolymer and / or the propylene / ethylene block copolymer composed of the propylene homopolymer portion and the propylene / ethylene copolymer portion is not particularly limited. Is appropriately selected.
As the propylene polymerization catalyst, a highly stereoregular catalyst is usually used. For example, a catalyst comprising a combination of a titanium trichloride composition obtained by reducing titanium tetrachloride with an organoaluminum compound and further treating with various electron donors and electron acceptors, an organoaluminum compound and an aromatic carboxylic acid ester ( JP-A-56-100806, JP-A-56-120712, JP-A-58-104907), and supported type in which titanium tetrachloride and various electron donors are brought into contact with magnesium halide. Examples thereof include catalysts (see JP-A-57-63310, JP-A-63-43915, and JP-A-63-83116). Furthermore, a metallocene-based catalyst as shown in WO-91 / 04257 is cited. The catalyst referred to as a metallocene catalyst may not contain alumoxane, but is preferably a catalyst in which a metallocene compound and an alumoxane are combined, a so-called Kaminsky catalyst.
[0068]
The propylene / ethylene block copolymer is produced by polymerizing propylene alone in the presence of the above catalyst by applying a production process such as a gas phase polymerization method, a liquid phase bulk polymerization method, or a slurry polymerization method, and then propylene and ethylene. Can be obtained by random polymerization. In order to obtain a propylene / ethylene block copolymer having the above-described melting characteristics (MFR), it is preferable to perform multistage polymerization by a slurry method or a gas phase fluidized bed method. Propylene can be homopolymerized in multiple stages, followed by random polymerization of propylene and ethylene. In the production of a propylene / ethylene block copolymer having many b unit parts, the gas phase fluidized bed method is particularly preferred.
[0069]
The propylene homopolymer is obtained by polymerizing propylene alone in the presence of the above catalyst by applying a production process such as a gas phase polymerization method, a liquid phase bulk polymerization method, or a slurry polymerization method. In order to obtain a propylene homopolymer having the above-described melting characteristics (MFR), it is preferable to perform multistage polymerization by a slurry method or a gas phase fluidized bed method.
[0070]
The mechanical properties of the propylene / ethylene block copolymer and the propylene homopolymer of the present invention preferably have a flexural modulus of 300 MPa or more, more preferably 500 to 3000 MPa, and still more preferably 1000 to 2000 MPa. If it is out of the above range, the rigidity is inferior and is not suitable as a structural material.
IZOD impact strength is preferably 1 kJ / m²Or more, more preferably 2 to 100 kJ / m²More preferably, it is 5-80 kJ / m², Particularly preferably 8 to 60 kJ / m²The range of is preferable. If it is less than the above range, the impact resistance is inferior and it is not suitable as a structural material.
[0071]
Even when the base material (B) of the present invention is blended with inorganic fillers such as talc, zinc white, glass fiber, titanium white, magnesium sulfate, pigments, etc., a coating film with particularly good adhesion should be formed. Can do.
[0072]
Moreover, the base material (B) of this invention can contain arbitrary additives and a compounding component in the range which does not impair the effect of this invention remarkably other than the above.
Specifically, pigments for coloring, antioxidants such as phenols, sulfurs and phosphoruss, antistatic agents, light stabilizers such as hindered amines, ultraviolet absorbers, various nucleating agents, dispersants, neutralizing agents , Foaming agents, copper damage inhibitors, lubricants, flame retardants, various resins other than the propylene-based block copolymer, and various rubber components such as polybutadiene and polyisoprene.
[0073]
Specifically, pentaerythryl-tetrakis [3- (3,5-di-t-butyl-4-hydroxylphenyl) propionate], octadecyl-3- (3,5-di-t-butyl-4-hydroxyphenyl) Propionate, tris- (3,5-di-t-butyl-4-hydroxybenzyl) -isocyanurate, triethylene glycol-bis [3- (3-t-butyl-5-methyl-4-hydroxylphenyl) propionate] Phenolic antioxidants such as tris (2,4-di-t-butylphenyl) phosphite, bis (2,4-di-t-butylphenyl) pentaerythritol diphosphite, tetrakis (2,4-di -T-butylphenyl) -4,4'-biphenylenediphosphonite and other phosphorus-based antioxidants, dimyristyl-3 3′-thiodipropionate, distearyl thiodipropionate, 2- (3-tert-butyl-5-methyl-2-hydroxyphenyl) -5-chlorobenzotriazole, 2- (3,5-di-t UV absorbers such as -butyl-2-hydroxyphenyl) benzotriazole, 2-hydroxy-4-n-octyloxybenzophenone, bis (2,2,6,6-tetramethyl-4-piperidyl) sebacate, bis (1 , 2,2,6,6-pentamethyl-4-piperidyl) sebacate, poly [{6- (1,1,3,3-tetramethylbutyl) amino-1,3,5-triazine-2,4-diyl} {(2,2,6,6-tetramethyl-4-piperidyl) imino} hexamethylene {(2,2,6,6-tetramethyl-4-piperidyl) imino}], bis 1-octyl-2,2,6,6-tetramethyl-4-piperidyl) sebacate, tetrakis (2,2,6,6-tetramethyl-4-piperidyl) 1,2,3,4-butanetetracarboxy Rate, tetrakis (1,2,2,6,6-pentamethyl-4-piperidyl) 1,2,3,4-butanetetracarboxylate, 2,4-di-t-butylphenyl-3,5-di Examples thereof include weather resistance stabilizers such as -t-butyl-4-hydroxybenzoate and antistatic agents such as glyceryl monostearate.
[0074]
The production method of the propylene-based resin composition constituting the substrate (B) of the present invention is not particularly limited, and the above-described blending components are blended into the propylene-based resin as necessary, and mixed and melted as necessary. It can be manufactured by kneading.
[0075]
In the present invention, the above-mentioned essential components, that is, a propylene homopolymer, and / or a propylene / ethylene block copolymer comprising a propylene homopolymer portion and a propylene / ethylene copolymer portion, and used as necessary. By blending optional ingredients, etc. in the above blending ratio, and kneading and granulating using a normal kneader such as a single screw extruder, twin screw extruder, Banbury mixer, roll mixer, Brabender plastograph, kneader, etc. A propylene-based resin composition constituting the substrate (B) of the present invention is obtained.
[0076]
In this case, it is preferable to select a kneading and granulating method capable of improving the dispersion of each component, and it is usually performed using a twin-screw extruder. In this kneading and granulation, the above-mentioned components may be kneaded at the same time, or a method of dividing and kneading each component may be employed to improve performance.
[0077]
The substrate (B) of the present invention can be obtained by molding using various known methods using crystalline polypropylene. For example, injection molding (including gas injection molding), compression molding, injection compression molding (press injection), extrusion molding, hollow molding, rotational molding, calendar molding, inflation molding, uniaxially stretched film molding, biaxially stretched film molding, etc. Various molded bodies can be obtained by molding. Among these, a molded body by injection molding, compression molding, or injection compression molding is preferable.
[0078]
The coated propylene-based resin molded article of the present invention does not contain halogen such as chlorine, and therefore has a low environmental load, excellent coating film adhesion, and has a physical property balance excellent in rigidity and impact resistance.
The coated propylene-based resin molded product of the present invention is used in various industrial parts fields, in particular, various molded products that are thinned, highly functional, and large in size, such as automotive parts such as bumpers, instrument panels, trims, garnishes, and televisions. Cases, washing machine tubs, refrigerator parts, air conditioner parts, vacuum cleaner parts and other household appliance parts, toilet seats, toilet seat covers, toilet parts such as water tanks, bathtubs, bathroom walls, ceiling parts, drain pans, etc. As a molding material for various industrial parts such as parts around the bathroom, it has sufficient performance for practical use.
[0079]
【Example】
EXAMPLES Next, although an Example and a comparative example demonstrate this invention further more concretely, this invention is not restrict | limited by these Examples, unless it deviates from the summary.
In the following examples and comparative examples, the physical properties and performance of the polymers were measured as follows. In each example, the catalyst synthesis step and the polymerization step were all carried out in a purified nitrogen atmosphere, and the solvent was dehydrated with molecular sieve (MS-4A) and then degassed by bubbling with purified nitrogen.
[0080]
(1) Molecular weight
A chromatographic analyzer (Waters GPC150CV type) was used. Orthodichlorobenzene was used as the solvent, and the measurement temperature was 135 ° C. The molecular weight was calculated by using a commercially available monodisperse polystyrene as a standard sample, creating a calibration curve for the retention time and molecular weight from the viscosity formula of the polystyrene standard sample and polypropylene, and calculating the molecular weight.
[0081]
(2) Pentad of propylene unit chain
350-500 mg of sample is completely dissolved in about 10 ml of NMR sample tube using about 2.2 ml of orthodichlorobenzene. Next, about 0.2 ml of deuterated benzene is added as a lock solvent and homogenized, and then measurement is performed at 130 ° C. by a proton complete decoupling method. The measurement conditions are a flip angle of 90 ° and a pulse interval of 5T1 or more (T1 is the longest value of the spin-lattice relaxation time of the methyl group). In the propylene polymer, since the spin-lattice relaxation time of the methylene group and methine group is shorter than that of the methyl group, the recovery of the magnetization of all the carbons is 99% or more under this measurement condition. In order to improve the quantitative accuracy,¹³It is preferable to perform integration for 20 hours or more using an NMR apparatus having a resonance frequency of C nucleus of 125 MHz or more.
[0082]
(3) Crystallinity
Measured by wide angle x-ray crystal diffraction and determined by multiple peak separation method (symmetric transmission method (2θ / θ = 5-60 °, 0.1 ° / step)).
(4) Melting point and heat of crystal melting
The melting point Tm and the heat of crystal fusion were determined by the following method using a thermal analysis system TA2000 manufactured by DuPont.
A sample (about 5 to 10 mg) is accurately weighed and placed in a dedicated aluminum pan. After melting at 200 ° C. for 3 minutes, the temperature is lowered to 30 ° C. at a rate of 10 ° C./minute, and then the melting curve is obtained by raising the temperature to 200 ° C. at 10 ° C./minute. The peak top temperature of was determined as the melting point. Further, the amount of heat calculated from the area surrounded by the peak and the baseline divided by the weight of the sample is defined as the amount of heat of crystal melting (J / g). When there is no clear peak corresponding to 1 J / g or more in the temperature range of 50 to 160 ° C. of the melting curve, n. d. Expressed as:
[0083]
(5) Elevated temperature elution fractionation with orthodichlorobenzene
Using an elution fractionator (CFC-T-102L manufactured by Mitsubishi Chemical Corporation), the elution temperature was determined as 100%. The elution fractionation was started from 5 ° C. and measured by increasing the temperature in increments of 4-5 ° C.
(6) Solubility test
A sample is charged into a solvent (heptane or toluene) in a separable flask with a stirring blade at a concentration of 10% by weight, and heptane is heated to an external temperature of 110 ° C. and toluene is heated to an external temperature of 120 ° C. to dissolve. Stirring is continued for 2 hours after the internal temperature becomes constant. Heptane is rapidly heated at the boiling temperature, and toluene is naturally cooled to 30 ° C., then the solution temperature is adjusted to 25 ° C., left to stand for 1 hour, and filtered through a SUS wire mesh No. 400. What remains in the wire mesh is insoluble, and what is passed as a solution is soluble, and is dried in a vacuum dryer at 80 ° C., 1 mmHg or less for 4 hours. Weigh and calculate the fraction of insoluble matter.

[0084]
(7) Non-tackiness
Evaluation was performed according to the following criteria by a finger-tackiness test.

(8) Flexural modulus
Using an injection molding machine with a clamping pressure of 100 tons, a test piece of 90 mm × 10 mm × 3 mm was molded by injection molding at a mold temperature of 40 ° C. and a cylinder temperature of 220 ° C., and the obtained injection molded piece was JIS- Based on K7203, measurement was performed at a test speed of 2 mm / min at 23 ° C. (unit: Mpa).
(9) Izod (IZOD) impact strength
The test piece was measured at 23 ° C. according to JIS-K7110 (unit: kJ / m²)did.
[0085]
(10) Interlayer adhesion test
A test piece of 150 mm × 70 mm × 2 mm was molded from a polypropylene manufactured by Nippon Polychem, using an injection molding machine (IS170 manufactured by Toshiba Machine Co., Ltd.) at a molding temperature of 220 ° C.
After forming the coating film by the method described below, a test piece with a grid pattern is prepared according to the grid pattern test method described in JIS-K5400, and an adhesive tape (registered trademark cello tape manufactured by Nichiban Co., Ltd.) Is attached to the grid of the test piece, and then pulled quickly in the vertical direction to peel off, and the number of grids that have not been peeled out of the 100 grids is counted as “number of residual grids / 100 ".
(11) Water resistance test
Hot water in which a coating film is formed on a base material using the paint component (A) or other polymer as a primer, a base coat is applied and baked on the coating film, and the coated material cured at room temperature is kept at 40 ° C. Soak in for 10 days. Then, after water | moisture content of the surface was dried, the adhesiveness test according to the cross cut test (JIS-K5400) was done like the said interlayer adhesiveness test.
[0086]
(12) Gasohol resistance test
Regular that formed paint film on base material using paint component (A) or other polymer as primer, painted base coat on the paint film, baked, and kept cured at room temperature at 20 ° C It was immersed in a gasoline: ethanol = 9: 1 mixed solution, and the time until significant peeling occurred on the coating film was measured.
[0087]
[Production Example 1]
(1) Synthesis of dichloro [dimethylsilylene (cyclopentadienyl) (2,4-dimethyl-4H-1-azulenyl) hafnium
(1) -1 Synthesis of ligand
2-Methylazulene (4.01 g) was dissolved in tetrahydrofuran (56 ml), cooled to 0 ° C. with an ice bath, and then 24.8 ml of methyl lithium in diethyl ether (1.14 mol / l) was added dropwise at the same temperature. did. After completion of dropping, the ice bath was removed and the mixture was stirred for 2 hours. This solution was slowly added dropwise to a tetrahydrofuran solution (140 ml) of dimethylsilyl dichloride (34.0 ml, 0.280 mol) cooled to 0 ° C. in an ice bath. After completion of the dropping, the ice bath was removed and the mixture was stirred for 3 hours, and then the solvent and unreacted dimethylsilyl dichloride were distilled off under reduced pressure. Tetrahydrofuran (80 ml) was added and the mixture was cooled to 0 ° C., and cyclopentadienyl sodium (2.1 mol / l, 26.9 ml, 56.5 mmol) was gradually added dropwise. After completion of the addition, the mixture was stirred at room temperature for 12 hours. After completion of the stirring, water was added and the target compound was extracted with diethyl ether. The extracted solution was dehydrated with magnesium sulfate and then dried to obtain an unpurified product of the target ligand. The crude product was purified by silica gel column chromatography using n-hexane as an elution solvent to obtain the target ligand (6.29 g) in a yield of 79%.
[0088]
(1) -2 Synthesis of complex
The ligand (6.29 g) obtained in (1) -1 was dissolved in tetrahydrofuran (100 ml) and cooled to 0 ° C. with an ice bath. At the same temperature, an n-hexane solution of n-butyllithium (1.56 mol / l, 28.4 ml) was slowly added dropwise. After completion of dropping, the ice bath was removed and the mixture was stirred for 3 hours, and the solvent was distilled off under reduced pressure. Toluene (60 ml) was added to the residue obtained after distilling off, followed by cooling to -78 ° C. A suspension of toluene (140 ml) in hafnium tetrachloride (7.17 g) cooled to -78 ° C was slowly added thereto. Thereafter, the cooling bath was removed and the mixture was stirred overnight. After completion of the stirring, the reaction solution was filtered using a G3 frit. The solid on the frit was further washed with toluene and the filtrate was concentrated to give a brown powder. The target complex was extracted from this brown powder with hot n-hexane (180 ml × 3 times). After the extract solution was dried to dryness, the obtained solid was suspended and washed with n-hexane (20 ml × 5 times) and then dried under reduced pressure to obtain the desired dichloro [dimethylsilylene (cyclopentadienyl). ) (2,4-dimethyl-4H-1-azulenyl) hafnium (2.90 g) was obtained (yield 25%).
Of the above compounds¹The results of H-NMR measurement are shown below.
¹H-NMR (CDCl_Three): δ0.85 (s, 3H), 0.86 (s, 3H), 1.47 (d, J = 7.1 Hz, 3H), 2.25 (s, 3H), 3.42-3.52 (m, 1H), 5.42 (dd, J = 4.7, 10.1 Hz, 1H), 5.80-5.85 (m, 2H), 5.90-5.95 (m, 1H), 6.16-6.20 (m, 2H), 6.65 (d, J = 11.4H), 6.80-6.85 (m, 1H), 6.98-7.02 (m, 1H).
[0089]
(2) Chemical treatment of clay minerals
Demineralized water (110 ml), magnesium sulfate heptahydrate (22.2 g) and sulfuric acid (18.2 g) were collected in a 1,000 ml round bottom flask and dissolved with stirring. In this solution, 16.7 g of granulated montmorillonite (Mizusawa Chemical Benclay SL) was dispersed, heated to 100 ° C. over 2 hours, and stirred at 100 ° C. for 2 hours. Then, it cooled to room temperature over 1 hour, and obtained slurry was filtered and the wet cake was collect | recovered. The collected cake was slurried again with demineralized water (500 ml) in a 1,000 ml round bottom flask and filtered. This operation was repeated twice. The finally obtained cake was dried at 110 ° C. overnight under a nitrogen atmosphere to obtain chemically treated montmorillonite (13.3 g).
[0090]
(3) Polymerization
A toluene solution of triethylaluminum (0.4 mmol / ml, 2.0 ml) was added to the chemically treated montmorillonite (0.44 g) obtained in (2), and the mixture was stirred at room temperature for 1 hour. Toluene (8 ml) was added to this suspension, and after stirring, the supernatant was removed. After repeating this operation twice, toluene was added to obtain a clay slurry (slurry concentration = 99 mg clay / ml).
In another flask, 0.114 mmol of triisobutylaluminum (manufactured by Tosoh Akzo) was collected, and the clay slurry (3.8 ml) obtained here and the complex (6) obtained in Production Example 1 (1) -2 were obtained. (0.02 mg, 11.4 μmol) of toluene diluted solution was added and stirred at room temperature for 10 minutes to obtain a catalyst slurry.
[0091]
Subsequently, toluene (750 ml), triisobutylaluminum (1.9 mmol) and liquid propylene (180 ml) were introduced into an induction stirring autoclave having an internal volume of 2 liters. The whole amount of the catalyst slurry was introduced at room temperature, the temperature was raised to 60 ° C., and the total pressure during polymerization was kept constant at 0.7 MPa, and stirring was continued for 1 hour at the same temperature. After completion of the stirring, unreacted propylene was purged to terminate the polymerization. The autoclave was opened and the whole toluene solution of the polymer was recovered, and the solvent and the clay residue were removed. As a result, 23.2 g of a propylene polymer was obtained. The results of analyzing the obtained polymer are summarized in Table 1. In the table, “n.d.” represents not detected.
[0092]
[Production Example 2]
As a material for clay slurry, 17.8 mg (34.2 mmol) of the complex, triisobutylaluminum (0.342 mmol) and clay slurry (11.4 ml) were used, and toluene (1100 ml) and triisobutylaluminum (0.5 mmol) were used. The procedure was the same as in Production Example 1, except that liquid propylene (264 ml), the polymerization temperature was 80 ° C., the total pressure was 0.8 Mpa, and the polymerization time was 1.83 hours. As a result, 245 g of a propylene polymer was obtained. The results of analyzing the obtained polymer are summarized in Table 1.
[0093]
[Production Example 3]
All operations were performed in the same manner as in Production Example 2, except that toluene (1350 ml), liquid propylene (90 ml), the polymerization temperature was 70 ° C., the total pressure was 0.31 Mpa, and the polymerization time was 2 hours. As a result, 44 g of a propylene polymer was obtained. The results of analyzing the obtained polymer are summarized in Table 1.
[0094]
[Production Example 4]
All operations were performed in the same manner as in Production Example 1 except that liquid propylene (182 ml) and triisobutylaluminum (0.5 mmol) were used. As a result, 39.6 g of a propylene polymer was obtained. The results of analyzing the obtained polymer are summarized in Table 1.
[0095]
[Production Example 5]
(1) Racemic synthesis of dichloro {1,1'-dimethylsilylenebis [2-ethyl-4- (2-fluoro-4-biphenylyl) -4H-azurenyl]} hafnium
2-Fluoro-4-bromobiphenyl (6.35 g, 25.3 mmol) was dissolved in a mixed solvent of diethyl ether (50 ml) and n-hexane (50 ml), and a solution of t-butyllithium in n-pentane (33 ml, 50 ml). .6 mmol, 1.54 N) was added dropwise at -78 ° C. The mixture was stirred at −10 ° C. for 2 hours, 2-ethylazulene (3.55 g, 22.8 mmol) was added to this solution, and the mixture was stirred at room temperature for 2 hours. n-Hexane (30 ml) was added and the supernatant was removed by decantation. This operation was repeated once more. N-Hexane (30 ml) and tetrahydrofuran (40 ml) were added to the obtained yellow precipitate at 0 ° C. Next, N-methylimidazole (50 ml) and dimethyldichlorosilane (1.4 ml, 11.4 mmol) were added, the temperature was raised to room temperature, and the mixture was stirred at room temperature for 1 hour. After this, dilute hydrochloric acid was added and the layers were separated, and then the organic phase was dried over magnesium sulfate. The solvent was distilled off under reduced pressure to obtain dimethylsilylenebis (2-ethyl-4- (2-fluoro-4-biphenyl) -1 , 4-dihydroazulene) (8.3 g) was obtained.
[0096]
Next, the crude product obtained above was dissolved in diethyl ether (30 ml), and an n-hexane solution of n-butyllithium (14.9 ml, 22.8 mmol, 1.53N) was added dropwise at -70 ° C. The temperature was gradually raised and the mixture was stirred overnight at room temperature. Furthermore, toluene (200 ml) was added, and the mixture was cooled to −70 ° C., hafnium tetrachloride (3.6 g, 11.4 mmol) was added, the temperature was gradually raised, and the mixture was stirred at room temperature for 4 hours. From the resulting slurry, most of the solvent was distilled off under reduced pressure, diethyl ether (50 ml) was added, and the resulting slurry was filtered. After washing with diethyl ether (5 ml × 2), ethanol (15 ml × 2), n-hexane (10 ml × 2), dichloro {1,1′-dimethylsilylenebis [2-ethyl-4- (2-fluoro-4 A racemic meso mixture (4.53 g, 42% yield) of -biphenylyl) -4H-azurenyl]} hafnium was obtained. The resulting racemic / meso mixture¹As a result of analysis by 1 H-NMR, it was found to be a mixture of racemic 76.6% and meso 23.4%.
The racemic / meso mixture (4.5 g) obtained here was suspended in dichloromethane (35 ml) and irradiated with light using a high pressure mercury lamp (100 W) for 1 hour. The solvent was distilled off under reduced pressure. Toluene (25 ml) and dichloromethane (11 ml) were added to the obtained solid, and the mixture was heated to 60 ° C. to obtain a homogeneous solution. When dichloromethane was distilled off under reduced pressure, crystals were precipitated. The obtained crystals were filtered, washed twice with hexane (5 ml), and dried under reduced pressure to obtain a racemate (1.79 g).
[0097]
(2) Chemical treatment of clay minerals
To a 500 ml round bottom flask, 55.85 g of demineralized water, 32.70 g of sulfuric acid and 8.01 g of lithium hydroxide were added and stirred. Treated under reflux for 140 minutes. After adding 300 ml of demineralized water and suction filtration, the solid component was dispersed in 600 ml of demineralized water and subjected to suction filtration. This operation was repeated once more. The residue obtained by filtration was dried at 100 ° C. to obtain acid and metal salt-treated montmorillonite.
1.05 g of the acid and metal salt-treated montmorillonite obtained here was collected in a 100 ml round bottom flask and dried by heating at 200 ° C. for 2 hours under reduced pressure. To this, 4.0 ml of a toluene solution of triethylaluminum (0.5 mmol / ml) was added under purified nitrogen, reacted at room temperature for 30 minutes, washed twice with 30 ml of toluene, and containing chemically treated montmorillonite. A toluene slurry was obtained.
[0098]
(3) Prepolymerization
Toluene was extracted from the toluene slurry obtained in (2) (containing 914.2 mg as a solid content) to make the residual toluene amount 1.0 ml. To this slurry was added a toluene solution of triisobutylaluminum (0.5 mmol / ml, 0.5 ml), and dichloro {1,1′-dimethylsilylenebis [2-ethyl-4- ( 2-Fluoro-4-biphenylyl) -4H-azurenyl]} hafnium in a toluene solution (3.0 mmol / ml, 9.2 ml) was added and stirred at room temperature for 1 hour to obtain a catalyst slurry.
Into a 2-liter induction stirring autoclave, 40 ml of toluene and the total amount of the catalyst slurry were introduced under purified nitrogen. 11.0 g of propylene was introduced with stirring, and prepolymerization was performed at 30 ° C. for 2 hours and then at 50 ° C. for 0.5 hour. After pre-polymerization, unreacted propylene was purged and pressure-replaced twice with purified nitrogen 0.5 MPa, and then the pre-polymerization catalyst was taken out. This contained 9.7 g of polymer per gram of chemically treated montmorillonite component.
[0099]
(4) Polymerization
A 2-liter induction-stirring autoclave containing a built-in stirring blade was replaced with purified nitrogen, and then 750 g of liquefied propylene was charged at 25 ° C. A toluene solution of triisobutylaluminum (0.1 mmol / ml, 5.0 ml) was injected at the same temperature, and then heated to 70 ° C. Hydrogen was added so that the hydrogen concentration in the gas phase was 0.2 mol%, and then 30.0 mg of the prepolymerized catalyst obtained in (3) above was added at 70 ° C. to initiate polymerization. After 1 hour, unreacted propylene was purged to complete the polymerization. The amount of the obtained propylene polymer was 384 g.
[0100]
The results of analyzing the obtained polymer are summarized in Table 1.
In addition,¹³Peak derived from carbon atom of methyl group of propylene unit chain part consisting of head-to-tail bond by C-NMR: [mmmm]> 99.9 (%), and few peaks derived from other pentads are seen It was.
[0101]
[Production Example 6]
Highly stereospecific isotactic polypropylene (31.1 g), heptane (180 ml), Pd / C (Aldrich: 10 wt% Pd / C) (7.87 g) in an induction-stirring microautoclave with an internal volume of 50 mL Was added, and the system was closed and replaced with nitrogen. Thereafter, 8.0 MPa of hydrogen was introduced, the temperature was raised to 275 ° C., and stirring was continued for 6 hours. After cooling, hydrogen was purged to stop the reaction. The autoclave was opened and the entire amount of the polymer heptane solution was recovered, and the solvent and the Pd / C residue were removed. As a result, 30.6 g of a propylene polymer was obtained.
The physical properties of the highly stereospecific isotactic polypropylene used are as follows.
MFR: 15,000 g / 10 min;
Tm: 154.9 ° C .;
Mw: 37,000; Mn: 18,000; Mw / Mn: 2.1;
[Mmmm]: 98.4%; [mmmmr]: 0.0%; [rmrm]: 0.1%; [rrrr]: 0.2%.
[0102]
[Reference Example 1]
The physical properties of Ziegler-Natta polypropylene (Ube Industries, Ubetak UT-2115) were measured in the same manner.
[0103]
In the following examples, the grade name, type, physical properties, etc. of the crystalline polypropylene used as the substrate (B) are shown in Table 2. All grade names are trade names of Nippon Polychem. In Table 2, the pentad fraction indicates mmmm pentad.
[0104]
[Table 1]

[0105]
[Table 2]

[0106]
[Example 1]
(1) Maleic anhydride modification of propylene polymer
Chlorobenzene (80 g), the propylene polymer (20 g) obtained in Production Example 1 (3) and maleic anhydride (4 g) are added to a stainless steel pressure-resistant reaction vessel equipped with a thermometer and a stirrer, and the inside of the vessel is filled with nitrogen gas. And heated to 132 ° C. After raising the temperature, 16 g of a chlorobenzene solution (10% by weight) of dicumyl peroxide (DCPO) was supplied for 5 hours using a metering pump, and then the reaction was continued for 3 hours at the same temperature. After completion of the reaction, the system was cooled to around room temperature, acetone was added, and the precipitated polymer was filtered off. Further, precipitation and filtration were repeated with acetone, and the finally obtained polymer was washed with acetone. The polymer obtained after washing was dried under reduced pressure to obtain a white powdery modified resin. As a result of performing infrared absorption spectrum measurement and neutralization titration of this modified resin, the graft amount (content of maleic anhydride group) was 3.3% by weight.
To 15 g of the maleic anhydride-modified propylene polymer obtained here was added 135 g of toluene, and the temperature was raised to 100 ° C. and dissolved for 1 hour. After cooling the obtained solution to near room temperature, a 10 wt% solution of maleic anhydride-modified propylene polymer was prepared through a # 400 SUS wire mesh.
[0107]
(2) Physical property evaluation of modified propylene polymer
The amount of the toluene solution of the maleic anhydride-modified propylene polymer obtained in (1) above was applied to an injection-molded test piece (with the surface wiped with isopropyl alcohol) prepared from various PP base materials shown in Table 2. 3-5g / m²Spray applied. Next, this molded test piece was allowed to stand at 25 ° C. for 1 hour, and then dried in a safe ben dryer at 80 ° C. for 30 minutes. Next, the dried product was allowed to stand at 25 ° C. for 1 hour, and then an acrylic polyol urethane paint (manufactured by Kansai Paint Co., Ltd .: trade name: Retan PG80III) was blended with a predetermined amount of a curing agent over the coating film. Then, adjust the viscosity with Ford Cup No. 4 with a special thinner, adjust the viscosity to 12 to 13 seconds, and then spray coat so that the dry coating amount is 50 to 60 g, in the Safe Ben dryer Was baked at 100 ° C. for 30 minutes. Furthermore, it left still at 25 degreeC for 10 days, and was cured. An interlayer adhesion test was performed on the obtained coated product. In addition, a water resistance test and a gasohol resistance test were also performed. The results are shown in Table 3 together with the following examples.
[0108]
[Example 2]
Except for reacting at 110 ° C. using toluene (80 g), the propylene polymer synthesized in Production Example 2 (20 g), 10 g of maleic anhydride, and 12 g of a toluene solution (10 wt%) of dicumyl peroxide (DCPO). Were modified with maleic anhydride in the same manner as in Example 1, a coated product was prepared using the modified polymer, and physical property evaluation tests were conducted in the same manner.
[0109]
[Example 3]
Except for using the propylene polymer synthesized in Production Example 2, maleic anhydride modification was performed in the same manner as in Example 1, and a coated product was prepared using the modified polymer. went.
[0110]
[Example 4]
Except for using the propylene polymer synthesized in Production Example 3, maleic anhydride modification was performed in the same manner as in Example 1, and a coated product was prepared using the modified polymer. went.
[0111]
[Example 5]
Except for using the propylene polymer synthesized in Production Example 4, maleic anhydride modification was performed in the same manner as in Example 1, and a coated product was prepared using the modified polymer. went.
[0112]
[Example 6]
Example 1 except that methacrylic acid (5 g) was used instead of maleic anhydride (4 g) and the addition amount of dichlorobenzene solution (10 wt%) of dicumyl peroxide (DCPO) was changed from 16 g to 5 g. In this way, a modified resin was obtained. As a result of measuring the infrared absorption spectrum of this modified resin, the graft amount (content of methacrylic acid group) was 1.1% by weight. A coated product was prepared using the modified polymer, and a physical property evaluation test was conducted in the same manner.
[0113]
[Example 7]
Except for using 2-hydroxyethyl methacrylate (HEMA, 5 g) instead of maleic anhydride (4 g) and changing the amount of dicumyl peroxide (DCPO) in chlorobenzene (10 wt%) from 16 g to 5 g. A modified resin was obtained in the same manner as in Example 1. As a result of measuring the infrared absorption spectrum of this modified resin, the graft amount (content of 2-hydroxyethyl methacrylate group) was 1.0% by weight. A coated product was prepared using the modified polymer, and a physical property evaluation test was conducted in the same manner.
[0114]
[Example 8]
Instead of maleic anhydride (4 g), 2-hydroxyethyl methacrylate (HEMA, 5 g) and styrene (St, 5 g) were used, and the addition amount of dicumyl peroxide (DCPO) in chlorobenzene (10 wt%) was 16 g. A modified resin was obtained in the same manner as in Example 1, except that the amount was changed from 5 to 5 g. As a result of measuring the infrared absorption spectrum of this modified resin, the content of 2-hydroxyethyl methacrylate group was 2.5% by weight. A coated product was prepared using the modified polymer, and a physical property evaluation test was conducted in the same manner.
[0115]
[Comparative Example 1]
Maleic anhydride modification was performed in the same manner as in Example 1 except that the propylene polymer synthesized in Production Example 5 was used. The graft amount of the modified propylene polymer was 3.4% by weight. When the solubility test was conducted, the solubility in toluene was poor and 96% or more insoluble matter was obtained, and the coating evaluation could not be performed. However, the non-tack property was excellent. The results are shown in Table 4 together with the following comparative examples.
[0116]
[Comparative Example 2]
Maleic anhydride modification was performed in the same manner as in Example 1 except that the propylene polymer synthesized in Production Example 6 was used. The graft amount of the modified propylene polymer was 3.5% by weight. When the solubility test was performed, the solubility in toluene was good, but the tackiness was great and the coating evaluation was not achieved. There was also a problem with tackiness.
[0117]
[Comparative Example 3]
Maleic anhydride modification was performed in the same manner as in Example 1 using Ziegler-Natta catalyst polypropylene (Ubekku UT-2115 manufactured by Ube Industries). The graft amount of the modified propylene polymer was 3.4% by weight. When the solubility test of toluene was conducted, the amount of insoluble matter was as large as 29.5% by weight, and the coating evaluation could not be performed. There was also a problem with tackiness.
[0118]
[Comparative Example 4]
Maleic anhydride modification was performed in the same manner as in Example 1 using a propylene / butene-1 copolymer (Tafmer XR-110T, manufactured by Mitsui Chemicals, Inc., propylene component: butene-1 component = 76: 24). The graft amount of the modified propylene polymer was 3.0% by weight. When the solubility test of toluene was conducted, the amount of insoluble matter was as high as 67.4% by weight, and the coating evaluation could not be performed. However, the non-tack property was excellent.
[0119]
[Comparative Example 5]
Coating evaluation was performed using maleic anhydride-modified chlorinated polypropylene (Eastman, CP-343-1) as a modified polymer. Non-tackiness was excellent, but particularly poor adhesion and water resistance.
[0120]
[Table 3]
[Table 3 (1)]

[0121]
[Table 4]
[Table 3 (2)]

[0122]
[Table 5]
[Table 4]

[0123]
【The invention's effect】
The polypropylene-based coated molded article of the present invention has a physical property balance that is excellent in coating film adhesion, and further excellent in rigidity and impact resistance. In addition, because it does not use halogens that are harmful to the global environment, it not only helps protect the global environment, but also significantly reduces the adverse effects of halogen on weather resistance, etc. As a result, the industrial value is extremely high because it is a technology development that brings about an extension of the life cycle and thus contributes to the saving of limited earth resources.

Claims (13)

A polypropylene-based paint molded article obtained by coating the base material (B) with the following paint component (A).
Coating component (A): a main chain comprising a propylene polymer having the following characteristics (1 ), (2) and (3) and satisfying the following requirement <1> , a carboxyl group, and a carboxylic acid anhydride group Or the coating component formed by containing the polar group containing propylene polymer which consists of a side chain containing a carboxylic acid ester group.
(1) Manufactured with a single site catalyst (2) When dissolved in heptane at 98 ° C. at a concentration of 10% by weight, the insoluble content is 1% by weight or less.
(3) Having a stereo block structure including both isotactic blocks and amorphous blocks.
<1> Ten types of pentads appearing in a range of 19.8 to 22.2 ppm when the stereoblock structure has a peak top chemical shift of 21.8 ppm attributed to a pentad represented by mmmm. The ratio (S ₁ / S) of the peak area S ₁ having a peak top of 21.8 ppm to the total area S of the peaks belonging to is 20 to 60%. Substrate (B): Crystallinity A molded product of polypropylene. The polypropylene-based coated molded article according to claim 1, wherein the stereo block structure satisfies the following requirement <2> .
<2> When the area of the peak (mmmr) having a peak top was S ₂ to 21.5～21.7Ppm, relationship S ₁ and S _{2 are, 4 + 2S 1 / S 2} > 5 be satisfied. The polypropylene-based coated molded article according to claim 1 or 2 , wherein the main chain composed of the propylene-based polymer has the following property (4).
(4) When dissolved in toluene at 25 ° C. at a concentration of 10% by weight, the insoluble content is 1% by weight or less. The polypropylene-based coated molded article according to any one of claims 1 to 3 , wherein the main chain composed of the propylene-based polymer has the following property (5).
(5) The weight average molecular weight Mw measured by GPC is 5,000 to 1,000,000. 5. The polypropylene according to claim 1, wherein the main chain made of the propylene-based polymer has a ratio (Mw / Mn) of the weight average molecular weight Mw to the number average molecular weight Mn of Mw / Mn <20. Painted molded body. The polypropylene-based coated molded article according to any one of claims 1 to 5 , wherein the main chain made of the propylene-based polymer has the following property (6).
(6) There is no clear peak corresponding to a crystal heat of fusion measured by DSC of 1 J / g or more.   The polypropylene-based coating according to any one of claims 1 to 6, wherein the crystalline polypropylene is a propylene homopolymer or a propylene / ethylene block copolymer comprising a propylene homopolymer portion and a propylene / ethylene copolymer portion. Molded body.   The polypropylene-based coated molded article according to claim 7, wherein the propylene homopolymer has an MFR of 2 to 300 g / 10 min.   The propylene homopolymer part of the propylene / ethylene block copolymer is 50 to 95% by weight, the propylene / ethylene copolymer part is 5 to 50% by weight, and the MFR of the propylene homopolymer part is 10 to 500 g / The polypropylene-based coated molded article according to claim 7, which is 10 minutes.   The polypropylene system according to claim 9, wherein the propylene homopolymer part is 60 to 90% by weight, the propylene / ethylene copolymer part is 10 to 40% by weight, and the MFR of the entire block copolymer is 2 to 300 g / 10 minutes. Painted molded body.   The polypropylene-based paint molded article according to claim 10, wherein the MFR of the entire block copolymer is 25 to 200 g / 10 min. The coating component (A) is a polar group-containing propylene polymer having a solubility parameter of 11 (cal / cm ^Three ) ^1/2 The polypropylene-based paint molded article according to any one of claims 1 to 11, which is a coating composition dissolved in 1% by weight or more in the following solvent. C with a single-site catalyst having a crosslinking group ₁ The polypropylene-based painted molded article according to any one of claims 1 to 12, which is a symmetric answer metallocene complex.