JP2004010735A - Filler for powder coating and powder coating composition comprising the same - Google Patents

Filler for powder coating and powder coating composition comprising the same Download PDF

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Publication number
JP2004010735A
JP2004010735A JP2002165255A JP2002165255A JP2004010735A JP 2004010735 A JP2004010735 A JP 2004010735A JP 2002165255 A JP2002165255 A JP 2002165255A JP 2002165255 A JP2002165255 A JP 2002165255A JP 2004010735 A JP2004010735 A JP 2004010735A
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Japan
Prior art keywords
powder coating
resin
calcium carbonate
filler
powder
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JP2002165255A
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Japanese (ja)
Inventor
Hidehiko Nishioka
西岡 英彦
Hiroshi Shibata
柴田 洋志
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Maruo Calcium Co Ltd
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Maruo Calcium Co Ltd
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Application filed by Maruo Calcium Co Ltd filed Critical Maruo Calcium Co Ltd
Priority to JP2002165255A priority Critical patent/JP2004010735A/en
Publication of JP2004010735A publication Critical patent/JP2004010735A/en
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a filler for powder coating which gives a powder coating composition for forming a coating film having good external appearance. <P>SOLUTION: The filler for powder coating comprises a surface treated calcium carbonate having a BET specific surface area by the nitrogen adsorption method of 2-15 m<SP>2</SP>/g, and the powder coating is obtained by compounding the calcium carbonate with a thermosetting resin. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、高外観の塗膜を形成する粉体塗料用充填剤及びそれを配合してなる粉体塗料樹脂組成物に関する。
【0002】
【従来の技術】
粉体塗装は静電スプレーや流動層浸漬塗装等の方法により、粉体塗料を空気中に飛翔あるいは空気中に浮遊させることにより被塗物に付着せしめてから焼き付けるなどして塗装をおこなう方法である。粉体塗装は無溶媒である粉体塗料を用いるため、溶剤型塗料を用いる塗装法のように溶媒が原因となる環境問題及び災害発生の危険性も無く、また水溶性塗料の場合に発生する排水処理問題もないこと、さらにはオーバースプレーされた塗料を回収して再使用することが可能であるため塗料の損失を非常に少なくできるという特徴があり、種々の塗装分野において広く用いられるようになってきている。
【0003】
また、回収装置と塗装機の組合せで完全循環システムによる自動化が可能であるので、塗装作業に熟練技能者を必要としないことも含めて、効率的な塗装が可能であるとされている。粉体塗装では、静電スプレー塗装や流動層浸漬塗装等の方法により被塗物に塗布され、焼き付けられることにより塗膜が形成される。
【0004】
しかしながら、従来の粉体塗料では、艶のある平滑な塗膜を形成することが出来ず、塗膜の外観に劣るという欠点がある。即ち、粉体塗料の造膜過程は、被塗物に塗着した粉体が、加熱溶融とそれに続く硬化を経て造膜する。その際の溶融流動と前後して硬化が進行するため、レベリング不足となり、塗膜外観が悪くなる傾向にある。その解決策として、塗膜を厚くし、焼き付け温度を高くしたり温度保持時間を長くして樹脂を十分に溶融させる必要があるが、粉末塗料の粒子の形状による僅かな凹凸を完全になくすのは困難である。特に、薄膜の塗装ではこの凹凸がより目立ち、塗膜の外観を一層悪くするという問題がある。
【0005】
この外観改良の要請は強く、これに対応するには、樹脂の溶融粘度を下げることが必要である。溶融粘度を下げる目的で、樹脂のガラス転移温度の低温化や分子量を低くするなどの方法が提案されているが、粉体で高平滑な塗膜を達成するために溶融粘度を低くした場合、焼き付け時にタレを生じ高外観の塗膜を得ることが出来ない場合があり、また塗装作業性も低下する。また、塗膜の平滑性を向上させる方法として厚膜化が効果的であるが、前述の溶融粘度を下げた樹脂と組み合わせた場合、焼き付け時のタレ現象が更に顕著となる。
【0006】
このような欠点を改善し、平滑な塗膜を得るための技術として、例えば、特開平2001−33750号公報には、粉体塗料の粒子状樹脂成分に加えて液状あるいは溶媒に溶解した液状樹脂成分を含有せしめた塗料組成物が開示されているが、塗装材料のコストが高くなることに加えて、無溶媒である粉体塗料の特徴がなくなり、装置コストや溶媒回収コストにも問題が生じる。また、特開平8−41384号公報には、搬送性に優れ高外観の塗膜を形成する粉体塗料として、塗膜形成用樹脂の体積平均粒径を20〜50μmとし、しかも粒度分布標準偏差が20μm以下である粉体塗料を用いることが開示されている。しかし、このように粒度分布を制御した粉体塗料を得るには、同公報にも例示されているように分級操作が必須となり、製造コストが高くなることが避けられない。また、同公報にはハイブリッド粉体塗料として、ガラス転移点の低い樹脂をガラス転移点が高い樹脂で被覆し、かつ前記粒度分布をなす粉体塗料も開示されているが、特定の樹脂の組み合わせに制限されることや、操作が複雑となり、さらなるコストアップとなる。
【0007】
【発明が解決しようとする課題】
本発明は、上記の従来技術の欠点を解消し、高外観の塗膜を形成する粉体塗料組成物を提供し得る粉体塗料用充填剤及び該充填剤を配合した粉体塗料組成物を提供するものである。
【0008】
【課題を解決するための手段】
本発明者らは上記課題を解決せんとして鋭意検討を重ねた結果、特定の粉体物性を有する炭酸カルシウムからなる充填剤が上記の如き従来の欠点を解消するとともに高外観の塗膜を与える粉体塗料を提供できることを見いだし、本発明を完成するに至った。
【0009】
本発明の第1は、窒素吸着法によるBET比表面積が2〜15m/gの炭酸カルシウムからなることを特徴とする粉体塗料用充填剤である(請求項1)。
【0010】
好ましい様態として、炭酸カルシウムの平均粒子径が0.5〜15μmである請求項1記載の粉体塗料用充填剤である(請求項2)。
【0011】
好ましい様態として、炭酸カルシウムが飽和脂肪酸、不飽和脂肪酸、脂肪族カルボン酸、樹脂酸、不飽和カルボン酸の(共)重合物、それらのアルカリ金属塩、それらのアルカリ土類金属塩、界面活性剤、シランカップリング剤から選ばれる少なくとも1種で表面処理されている請求項1又は2記載の粉体塗料用充填剤である(請求項3)。
【0012】
好ましい様態として、表面処理率が炭酸カルシウムの単位BET比表面積当たり0.05〜0.50重量%/mである請求項1〜3のいずれか1項に記載の粉体塗料用充填剤である(請求項4)。
【0013】
本発明の第2は、請求項1〜4のいずれか1項に記載の粉体塗料用充填剤を粉体塗料樹脂に配合してなることを特徴とする粉体塗料組成物である(請求項5)。
【0014】
好ましい様態として、粉体塗料樹脂が熱硬化性樹脂である請求項5記載の粉体塗料組成物である(請求項6)。
【0015】
好ましい様態として、熱硬化性樹脂がポリエステル樹脂、エポキシ樹脂、エポキシ−ポリエステル樹脂、フッ素樹脂、アクリル樹脂から選ばれる少なくとも1種からなる請求項6記載の粉体塗料組成物である(請求項7)。
【0016】
好ましい様態として、粉体塗料用充填剤の配合量が粉体塗料樹脂100重量部に対し1〜75重量部である請求項5〜7のいずれか1項に記載の粉体塗料組成物である(請求項8)。
【0017】
【発明の実施の形態】
本発明の粉体塗料用充填剤は、窒素吸着法によるBET比表面積が2〜15m/gである炭酸カルシウムからなることを特徴とする。
【0018】
炭酸カルシウムには、一般に、石灰石を機械的に粉砕し、該炭酸カルシウムを分級することにより各種グレードに調整される重質炭酸カルシウムと、化学的方法により調製される合成炭酸カルシウムの2種に大別される。更に、後者は、▲1▼石灰石を高温で焼成して得られる生石灰と水とを反応させて石灰乳を調整後、石灰乳中に石灰石焼成時に発生する炭酸ガスを導通させ炭酸カルシウムを合成する炭酸ガス化合プロセス、▲2▼石灰乳に炭酸ソーダを反応させる石灰ソーダプロセス、▲3▼可溶性のカルシウムと可溶性炭酸塩を反応させる溶液法の3種がある。
【0019】
本発明の充填剤を構成する炭酸カルシウムは特に制限されないが、上記重質炭酸カルシウムはその製法上の理由から粒度分布がブロードであるので光沢が低下する場合がある。従って、一定以上の微細度を有する炭酸カルシウムを特殊な分級(分級を何度も繰り返す)することによって所望の粒度分布として使用することが望ましい。
【0020】
また、合成炭酸カルシウムについては、上記▲2▼の石灰乳に炭酸ソーダを反応させる石灰ソーダプロセス及び▲3▼の可溶性のカルシウムと可溶性炭酸塩を反応させる溶液法は、その反応の特徴上、副産物としてNaCl等が生成され、その除去のためにコスト高となるので好ましくない場合がある。
【0021】
一方、上記▲1▼の炭酸ガス化合プロセスは、一般的に経済的な観点から好ましいが、該炭酸ガス化合プロセスを用いて製造された合成炭酸カルシウムは一次粒子形状が比較的揃っており、通常一次粒子が凝集または集合し、二次粒子(一次粒子の凝集体粒子)を形成している。本発明の充填剤を構成する炭酸カルシウムとしては、一次粒子径が揃っている合成炭酸カルシウム(コロイド炭酸カルシウム)が特に好ましい。
【0022】
本発明に用いられる炭酸カルシウムのBET比表面積は、2〜15m/gである必要があり、好ましくは3〜13m/gであり、更に好ましくは4〜10m/gである。炭酸カルシウムのBET比表面積が2m/g未満であると、体質顔料自体の一次粒子径が大きくなり、該粉体塗料を用いて塗膜にした場合、塗膜表面の平滑性が損なわれ外観、特に光沢が損なわれる。一方、15m/gを超える場合は、炭酸カルシウムの一次粒子径が小さくなり、凝集性が強くなり樹脂に配合するときに充分に分散されない場合や、必要以上に樹脂等を吸着し、粉体塗料の加熱溶融時のレベリングを悪くし、出来上がり塗膜の外観が損なわれる。
【0023】
粉体塗料を使用して得られる塗膜が優れた外観(光沢)を有するためには、塗料が通常の塗料とは異なり、塗料粉体の凝集エネルギーが物性の低下を招くと考えられる。その中に配合される炭酸カルシウムは、一次粒子径が小さい程BET比表面積が高くなる。BET比表面積が高くなるに従って塗料粉体の凝集エネルギーが大きくなり、外観不良が起こると考えられる。一方、BET比表面積が低い(一次粒子が特定以下に大きい)と平滑性が損なわれ、外観特に光沢を損なわれると考えられる。
【0024】
また、粉体塗料の凝集は粉体粒子の粒子径に影響され、粒子サイズが小さくなればなるほど、その凝集力は強くなる。そこで、粉体塗料ではその凝集を防ぐために通常の溶剤系塗料とは違い、表面調整剤等の薬剤が含有されている。その中に、前述のBET比表面積が比較的大きい炭酸カルシウムを配合した場合、該炭酸カルシウムが薬剤等を吸着してしまい表面調整等の機能を充分に発揮しなくなり、塗料粉体自体が凝集し高外観の塗膜を得ることが出来ないと考えられる。従って、炭酸カルシウムのBET比表面積は、上記した範囲に調整される必要がある。
【0025】
また、本発明に用いられる炭酸カルシウムは、通常一次粒子が凝集または集合し、二次粒子(一次粒子の凝集体粒子)を形成しているので、粉体塗料用の炭酸カルシウムとしては、特定の平均粒子径(二次粒子としての粒度構成)を満足することが好ましく、これによって塗料粉体の再凝集性を防止し、粉体塗料を塗装した場合に優れた外観を得ることができる。
【0026】
即ち、本発明に用いられる炭酸カルシウムの平均粒子径は、0.5〜15μmであることが好ましく、より好ましくは、0.75〜12μm、更に好ましくは1.0〜10μmである。平均粒子径が0.5μm未満では、凝集性が強くなり樹脂に配合するときに十分な分散が得られない場合や、必要以上に塗料樹脂や添加剤等を吸着し、粉体塗料の加熱溶融時のレベリングを悪くし、出来上がり塗膜の外観を損なう場合があるため好ましくない。一方、15μmを超えると、該粉体塗料を用いて塗膜にした場合、塗膜表面の平滑性が損なわれ、外観、特に光沢を損なう場合があるため好ましくない。
【0027】
尚、該平均粒子径は、下記条件にて測定を行った。
粒度分布測定条件:下記の配合材(I)と(II)を140mlマヨネーズ瓶に秤量し、ステンレススプーンにて目視分散するまで撹拌し、配合剤(III)で希釈後、超音波分散機にて予備分散させたものを試料とし、レーザー回折式粒度分布計(島津製作所社製:SALDー2000)により測定を行った。
(I)中性洗剤(水で5倍希釈したもの) 2.0g
(II)炭酸カルシウム試料        0.4g
(III)水                                 40g
尚、前処理として前記した配合で調整後、超音波分散機US−300T(日本精機製作所社製)を用い100μA−60秒間の一定条件にて予備分散させた。また中性洗剤は、特に限定されるものでなく一般の市販品で問題なく、本発明ではママレモン(ライオン社製)を使用した。
【0028】
本発明に使用する炭酸カルシウムは、例えば水酸化カルシウム水懸濁液(以下石灰乳という)に炭酸ガス含有ガス(以下炭酸ガスという)を導通する方法、あるいは炭酸ガス中に石灰乳または水酸化カルシウムと沈降性炭酸カルシウムとの混合液を噴霧する方法等の公知の方法で製造される。また、炭酸カルシウム粒子はできるだけ分散させておくのが好ましいが、その方法としては、例えば炭酸化反応を反応系のpHを7.5〜10.0で停止し、攪拌を行い炭酸カルシウム中に残存するアルカリ分を溶出させ、石灰乳と炭酸ガスを必要に応じて系内に添加または導通し系のpHを9.0〜12.0で5時間以上コントロールする方法が挙げられる。
【0029】
また、微細な重質炭酸カルシウムを得るには、天然に産出される石灰石を乾式もしくは湿式で粉砕し、平均粒子径0.4〜1.0μmの微細な粒子に調整する。乾式の場合はミクロンミル、振動ボールミル等で粉砕後、風力分級機で分級し、湿式の場合はボールミルやタワーミル等の連続湿式分散機で粉砕すれば良く、特に制限されない。
【0030】
本発明に用いられる炭酸カルシウムは、表面活性を向上させ、粉体塗料樹脂との親和性を良くするために表面処理を行うのが好ましい。
【0031】
表面処理剤としては、飽和脂肪酸、不飽和脂肪酸、脂環族カルボン酸、樹脂酸及びそれらのアルカリ金属塩、アルカリ土類金属塩類、界面活性剤、シランカップリング剤、高分子系(共)重合物、そのアルカリ金属塩、そのアルカリ土類金属塩等が挙げられる。具体的には、カプリル酸、ラウリン酸、ミリスチン酸、パルミチン酸、ステアリン酸、アラギン酸等の飽和脂肪酸、オレイン酸、エライジン酸、リノール酸、リシレイン酸等の不飽和脂肪酸、ナフテン酸等の脂環族カルボン酸、アビエチン酸、ピマル酸、パラストリン酸、ネオアビエチン酸等の樹脂酸が挙げられ、それらのアルカリ金属、アルカリ土類金属、NH、Al、Zn等による部分もしくは完全中和塩が挙げられる。また、ドデシルベンゼンスルホン酸、スルホコハク酸ジアルキルエステル及びそれらのNa塩等に代表されるようなスルホン酸型、硫酸ドデシルナトリウムなどに代表されるような硫酸エステル型、モノラウリルリン酸ナトリウム、硫酸ドデシルポリオキシエチレン及びその塩等に代表されるようなリン酸エステル型などのアニオン系界面活性剤、ステアリルアミン塩酸に代表されるようなアミン塩型、ステアリルトリメチルアンモニウムクロリドに代表されような第4級アンモニウム塩型などのカチオン型界面活性剤、グリセリンモノステアリン酸エステルに代表されるようなエステル型、ポリオキシエチレンノニルフェニルエーテルに代表されるようなエーテル型、ポリエチレングリコールオレイン酸エステルに代表されるようなエステルエーテル型、ラウリン酸ジエタノールアミドに代表されるような、アルカノールアミド型などの非イオン系界面活性剤、ビニルシラン、アミノシラン、エポキシシラン、クロロアルキルシラン、メチルトリエトキシシランなどのシランカップリング剤などが挙げられる。更に、アクリル酸、イタコン酸、マレイン酸等の不飽和モノカルボン酸、不飽和ジカルボン酸等からなる単量体の重合物やそれらと共重合可能な単量体との共重合物のアルカリ金属、アルカリ土類金属、NH、Al、Zn等による部分もしくは完全中和塩等が挙げられる。これらの表面処理剤は、単独で処理を行ってもよいが、2種以上を併用して処理を行っても良い。これらの中で、飽和脂肪酸のアルカリ金属塩、樹脂酸のアルカリ金属塩が炭酸カルシウムとの反応性が良く、工業的に入手し易い点で好ましい。
【0032】
表面処理剤の処理量は炭酸カルシウム粒子を均一に表面処理できれば良く、用いる粉体塗料樹脂の種類により適宜選択すれば良いが、単位面積あたりの処理率として、単位BET比表面積に対して0.05〜0.50重量%であるのが好ましく、より好ましくは0.07〜0.40重量%である。0.05重量%未満の場合、単位BET比表面積に対する処理量が少なくなり、表面処理を施した効果が充分に発揮できず好ましくない場合がある。0.5重量%を超えると、単位BET比面に対する処理量が多くなり、過剰な表面処理剤が塗料用樹脂の物性に悪影響をおよぼしたり、過剰な表面処理剤が造膜時の焼き付け時に溶融し塗膜を白濁させたりする場合があり好ましくない。
【0033】
表面処理した炭酸カルシウムを粉体として得る方法は常法によればよいが、例えば既述の製法により得られた平均粒子径0.01〜1.0μmの炭酸カルシウムスラリー中に添加し、攪拌等により均一に混合して炭酸カルシウム粒子に該表面処理剤を吸着させた後、フィルタープレス等で脱水、乾燥、粉末化することにより得ることができる。また炭酸化完了の炭酸カルシウムスラリーを一旦脱水し、該表面処理剤を炭酸カルシウムのプレスケーキに添加、強力に攪拌した後、スプレードライヤー等で乾燥、粉末化して得ることができる。さらに炭酸カルシウム表面に強固に固着させる方法としては、該表面処理剤を添加した炭酸カルシウムスラリーを乾燥前にサンドグラインダー等の連続湿式分散機で分散させるのも効果的である。
【0034】
本発明の粉体塗料組成物は、上記の如くして得られる本発明の粉体塗料用充填剤を粉体塗料樹脂に配合して得られる。粉体塗料樹脂としては特に限定されず、粉体塗料分野において通常使用されるものを使用することができ、このようなものとしては、例えば、熱可塑性樹脂、熱硬化性樹脂等を挙げることができる。熱可塑性樹脂としては特に限定されないが、特に、ポリ塩化ビニル樹脂等のビニル樹脂、ポリエチレン樹脂、ポリアミド樹脂、フッ素樹脂等を好適に使用することができる。熱硬化性樹脂としては特に限定されないが、特に、エポキシ樹脂、エポキシ−ポリエステル樹脂、アクリル樹脂、フッ素樹脂、ポリエステル樹脂等を好適に使用することができる。塗料樹脂として熱硬化性樹脂を使用する場合、本発明の粉体塗料組成物は、硬化剤、硬化促進剤を含有することが好ましい。
【0035】
本発明の粉体塗料用充填剤の配合量は、粉体塗料樹脂100重量部に対して1〜75重量部、好ましくは5〜70重量部、更に好ましくは10〜50重量部である。粉体塗料用充填剤の配合量が1重量部未満では充分な添加効果が得られず、一方、75重量部を超えると、樹脂に練り込む際に粉体塗料自体を形成できない場合や粘度が高くなりすぎて作業性が悪くなったり、塗膜自体を形成しない場合があるので好ましくない。
【0036】
本発明の粉体塗料組成物において、耐候性の良好な塗膜を形成する必要がある場合にはアクリル樹脂系を、また耐衝撃性等の塗膜物性が良好な塗膜を形成する必要がある場合にはポリエステル樹脂系を、更に、耐食性の良好な塗膜を形成する必要がある場合にはエポキシ樹脂を用いることが好ましい。また、必要に応じ、ガラス転移点の低い樹脂をガラス転移点の高い樹脂で被覆する等、2種以上の樹脂を併用してもよい。
【0037】
本発明においては、粉体塗料樹脂としてエポキシ樹脂を使用する場合には、必要により、例えば、無水フタル酸、アミン化合物、イミダゾール化合物、ジシアンジアミド等の硬化剤、硬化促進剤を使用することができ、またアクリル樹脂等の他の樹脂を併用することができる。また、粉体塗料樹脂として熱硬化性アクリル樹脂を使用する場合には、必要により、例えば、エポキシ樹脂、メラミン樹脂等の他の樹脂や、多価カルボン酸、ブロックイソシアネート化合物等の硬化剤を使用することができる。
【0038】
本発明においては、粉体塗料樹脂として熱硬化性ポリエステル樹脂を使用する場合には、必要により、例えば、メラミン樹脂、エポキシ樹脂等の他の樹脂や、多塩基酸、ブロックイソシアネート化合物、トリグリシジルイソシアヌレート等の硬化剤を使用するができる。
【0039】
上記硬化剤の含有量は、粉体塗料樹脂として使用される熱硬化性樹脂100重量部あたり、5〜80重量部が好ましい。5重量部未満であると硬化が不充分となり、80重量部を超えると硬化が進みすぎ、塗膜物性が低下する。また、上記硬化促進剤の含有量は、粉体塗料樹脂として使用される熱硬化性樹脂100重量部あたり0.1〜5重量部が好ましい。0.1重量部未満であると硬化が不充分となり、5重量部を超えると硬化が進みすぎ、塗膜物性が低下する傾向がある。
【0040】
本発明の粉体塗料組成物は、必要により、顔料、その他の添加剤を含んでいてもよい。上記その他の添加剤としては、他の樹脂、硬化剤、硬化促進剤又は硬化触媒、表面調整剤、可塑剤、紫外線吸収剤、酸化防止剤、ワキ防止剤、顔料分散剤等を挙げることができる。上記顔料としては特に限定されず、なかでも、二酸化チタン、べんがら、黄色酸化鉄、カーボンブラック、フタロシアニンブルー、フタロシアニングリーン、キナクリドン系赤色顔料等を好適に使用することができる。これらは単独で又は必要に応じ2種以上組み合わせて用いられる。
【0041】
上記顔料の含有量は、粉体塗料組成物100重量部に対して、1〜60重量部が好ましい。含有量が1重量部未満であると、着色等の顔料の効果が得られず、60重量部を超えると、高外観の塗膜が得られない。上記顔料及びその他の添加剤は、粉体塗料の粒子中に粉体塗料樹脂等とともに含まれていてもよく、また粉体塗料樹脂とは別の粒子として添加されていてもよい。
【0042】
粉体塗料樹脂の粒子は、例えば、乳化重合、懸濁重合等の方法により直接製造できる。また、溶液重合、塊状重合等により樹脂を製造し、これを粉砕して分級することにより得ることもできる。
【0043】
本発明の粉体塗料組成物の製造方法としては特に限定されず、粉体塗料製造分野において通常使用される方法等によって行うことができる。例えば、上述の粉体塗料樹脂、及び、必要に応じて使用される顔料、その他の添加剤をヘンシェルミキサー、スーパーミキサー、ボールミル、バンバリーミキサー等の混合機により均一に混合し、次に、得られた混合物を、エクストルーダーや熱ロール等の混練機により溶融混練し、溶融した粉体塗料樹脂中に樹脂以外の成分を均一に分散させ、得られた混合物をペレットに成形する。得られたペレットを、ハンマーミル等の衝撃型粉砕機、ジェットミル等の気流粉砕機等によって粉砕した後、分級することにより本発明の粉体塗料組成物が得られる。
【0044】
上記分級は、170メッシュ、好ましくは200メッシュのタイラー標準ふるい、90μm、好ましくは80μmよりも大きい粒子を分離し除去するディスパージョンセパレーター、ミクロンセパレーター等の流体分級機、及び、1μmよりも小さい粒子を分離し除去するサイクロン、ディスパージョンセパレーター、ミクロンセパレーター等の流体分級機等を使用して行うことができる。
【0045】
本発明の粉体塗料組成物の製造方法としては、上述の方法以外に、例えば、原料を溶剤中で混合し、得られた混合物を乾燥、微粉砕するか、又は、スプレードライ法により粉末にする方法を採用することもできる。得られた粉末は必要に応じて、上述の粉砕、分級に供することができる。
【0046】
このような粉体塗料用原料を用いると、樹脂成分中に顔料や各種添加剤が均等に分散したペレットが得られるので、ペレットの粉砕により得られる粉体塗料は、各粒子中に各種原料成分がほぼ均等に含まれることになる。このため、塗膜の形成工程において、例えば、樹脂の硬化反応が均一に起こり易くなるため、平滑性等の外観がより良好な塗膜を形成することができる。
【0047】
本発明の粉体塗料組成物の適用対象としては特に限定されず、例えば、自動車用、家電機器用、建材用、雑貨用等の鋼板、リン酸亜鉛処理鋼板、アルミニウム又はアルミニウム合金材等を挙げることができる。本発明の粉体塗料組成物の塗装方法としては、例えば、静電スプレー法、流動浸漬法等の周知の方法により本発明の粉体塗料組成物を被塗物の表面に所望の厚みで堆積させ、その後焼き付けることにより行うことができる。樹脂成分として熱硬化性樹脂を使用した場合には、硬化した塗膜が形成される。
【0048】
【実施例】
以下に実施例を掲げて本発明をさらに詳しく説明するが、本発明はこれら実施例のみに限定されるものではない。
【0049】
実施例1
比重1.06の石灰乳を15℃に調整し、水酸化カルシウム1kgあたり30リットル/分の炭酸ガス(内25%CO)を導通し炭酸化反応を行い、系のpHが8.5となったときに炭酸化反応を停止した後に、系のpHを10〜11の条件下、50℃で24時間攪拌し、これにより凝集体粒子の極めて少ない平均一次粒子径が0.10μm、BET比表面積が11m/gの炭酸カルシウムからなる水スラリーを得た。この炭酸カルシウムスラリーに比重1.06、温度16℃の石灰乳を投入し、水酸化カルシウム1kgあたり3リットル/分の炭酸ガス(内25%CO)を導通し系のpHが8.5となるまで炭酸化反応を行った。得られた炭酸カルシウムスラリー中に更に前述と同様に調整された石灰乳を投入し、同様の操作により炭酸カルシウムスラリーを得た。この操作を数回繰り返すことにより、凝集粒子の極めて少ないBET比表面積が6.5m/g、平均粒子径3.17μmの炭酸カルシウムスラリーを得た。この炭酸カルシウムスラリーにアビエチン酸カリウムの濃度10%溶液を炭酸カルシウム固形分に対して処理率0.20%/mとなるように添加し、表面処理を行った後、フィルタープレスで脱水し、乾燥、解砕を行い、粉体塗料用充填剤を得た。
【0050】
実施例2
比重1.06の石灰乳を15℃に調整し、水酸化カルシウム1kgあたり30リットル/分の炭酸ガス(内25%CO)を導通し炭酸化反応を行い、系のpHが8.5となったときに炭酸化反応を停止した後に、系のpHを10〜11の条件下、50℃で24時間攪拌し、再び炭酸ガスを導通して系のpHを6.8とした。これにより凝集体粒子の極めて少ない平均一次粒子径が0.10μm、BET比表面積が11m/g、平均粒子径4μmの炭酸カルシウムからなる水スラリーを得た。この炭酸カルシウムスラリーにアビエチン酸カリウムの濃度10%溶液を炭酸カルシウム固形分に対して処理率0.25%/mとなるように添加し、表面処理を行った後、フィルタープレスで脱水し、乾燥、解砕を行い、粉体塗料用充填剤を得た。
【0051】
実施例3
比重1.06の石灰乳を15℃に調整し、水酸化カルシウム1kgあたり30リットル/分の炭酸ガス(内25%CO)を導通し炭酸化反応を行い、系のpHが8.5となったときに炭酸化反応を停止した後に、系のpHを10〜11の条件下、50℃で15時間攪拌しスラリー系の粘度が2300cpに達したとき、再び炭酸ガスを導通して系のpHを6.8とした。これにより凝集体粒子の極めて少ない平均一次粒子径が0.07μm、BET比表面積が14m/g、平均粒子径4μmの炭酸カルシウムからなる水スラリーを得た。この炭酸カルシウムスラリーにステアリン酸ナトリウムからなる濃度10%溶液を炭酸カルシウム固形分に対して処理率0.25%/mとなるように添加し、表面処理を行った後、フィルタープレスで脱水し、乾燥、解砕を行い、粉体塗料用充填剤を得た。
【0052】
実施例4
天然に産出される石灰石をミクロンミルで粉砕後、風力分級機で分級作業を繰り返し、平均粒子径2.0μmの粒子を得た。その後、ヘンシェルミキサーを用いてアビエチン酸カリウムを炭酸カルシウム固形分に対して処理率0.25%/mになるように表面処理を行い、粉体塗料用充填剤を得た。
【0053】
実施例5
実施例1において、炭酸ガス流量を3リットル/分を10リットル/分に変更することにより、BET比表面積6.5m/g、平均粒径6.5μmの炭酸カルシウムを得、続いて実施例1と同様の表面処理を行い、粉体塗料用充填剤を得た。
【0054】
実施例6
実施例1において、炭酸ガス流量を3リットル/分を15リットル/分に変更することにより、BET比表面積5.2m/g、平均粒径12.5μmの炭酸カルシウムを得、表面処理剤をステアリン酸ナトリウムに変更した以外は同様の操作を行い、粉体塗料用充填剤を得た。
【0055】
実施例7
実施例1において、、表面処理剤をステアリン酸ナトリウムに変えて処理率を0.08%/mに変更した以外は同様の操作を行い、粉体塗料用充填剤を得た。
【0056】
実施例8
実施例1において、表面処理剤をステアリン酸ナトリウムに変えて処理率を0.04%/mに変更した以外は同様の操作を行い、粉体塗料用充填剤を得た。
【0057】
実施例9
天然に産出される石灰石をミクロンミルで粉砕後、風力分級機で分級作業を繰り返し、BET比表面積5.2m/g、平均粒子径3.7μmからなる粉体塗料用充填剤を得た。
【0058】
比較例1
実施例1において、炭酸化終了後の熟成時間を10時間と変更した以外は同様の操作を行い、BET比表面積18m/g、平均粒子径2μmの炭カルスラリーを得た。その後、実施例1と同様の方法でアビエチン酸カリウムを炭酸カルシウム固形分に対して処理率0.2%/mになるように表面処理を行い、粉体塗料用充填剤を得た。
【0059】
比較例2
天然に産出される石灰石をミクロンミルで粉砕後、風力分級機で分級作業を繰り返し、BET比表面積2.5m/g、平均粒子径25μmの炭酸カルシウム粒子を得た。その後、ヘンシェルミキサーを用いてアビエチン酸カリウムを炭酸カルシウム固形分に対して処理率0.25%/mになるように表面処理を行い、粉体塗料用充填剤を得た。
【0060】
実施例1〜9及び比較例1、2で得られた粉体塗料用充填剤の特性を表1に示す。
【0061】
【表1】

Figure 2004010735
【0062】
実施例10〜22、比較例3〜5
実施例1〜9、比較例1〜2によって得られた粉体塗料用充填剤を用いて、下記要領にて各粉体塗料組成物を作成し、その塗料物性試験を行った。
【0063】
Figure 2004010735
【0064】
Figure 2004010735
【0065】
Figure 2004010735
【0066】
原料として上記成分をスーパーミキサー(日本スピンドル製造社製)にて約3分間混合し、コニーダー(ブス社製)により約100℃の条件で溶融混練した。室温で冷却し、粗粉砕後にアトマイザー(不二パウダル社製)で粉砕し、150メッシュの篩いで分級し、体積平均粒子径35μmの粉体塗料を得た。
【0067】
以上の方法にて製造した各粉体塗料を200×100×0.8mmのリン酸亜鉛処理を施した鋼板に、膜厚約60μmになるようにコロナ帯電型塗装ガンにより静電吹きつけ塗装し、180℃×20min、200℃×20minの各条件で焼き付けたのち、室温迄放冷した。塗膜性能の評価を下記の方法により行った。
【0068】
<外観評価>
◎ :凹凸が少なく、平滑な塗膜状態である。
○ :凹凸がややあるが、平滑な塗膜状態である。
△ :凹凸がややあり、ブツが僅かにある。
× :凹凸があり、平滑性にやや劣る。
××:ブツ等があり、平滑性に劣り、試験板の下部エッジ部分にたまりが認められる。
【0069】
<ペレットフロー値>
錠剤成形器を用い、各粉体塗料を300kg/cmの圧力で、直径50mmの円盤状のペレットに加圧形成した。このペレット1を、図1に示すように、200×100mmの金属製板に両面テープで固定し、この金属製板2を垂直に吊した状態で、180℃×20min焼き付け、ペレット1の流動した塗料長さ3を測定した。以上の試験を3回行い、その平均値を評価値とした。
【0070】
<光沢値>
上記した如く、180℃×20min、200℃×20minで焼き付けた各試験板の塗膜面のうち任意の5カ所を選択し、そのグロスメーター(日本電色(株)製)にて60°光沢、20°光沢をそれぞれ測定し、その平均値を評価値とした。
【0071】
【表2】
Figure 2004010735
【0072】
【発明の効果】
以上のように、本発明の粉体塗料用充填剤は、優れた外観を有する塗膜を形成する粉体塗料組成物を提供することができる。
【図面の簡単な説明】
【図1】ペレットフロー値の測定方法を示す説明図である。
【符号の説明】
1 ペレット
2 金属製板
3 塗料流動長さ[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a filler for a powder coating which forms a coating film having a high appearance, and a resin composition for a powder coating obtained by blending the same.
[0002]
[Prior art]
Powder coating is a method in which the powder coating is applied to the object by flying or floating in the air by electrostatic spraying or fluidized bed immersion coating, etc., and then baked, etc. to perform coating. is there. Since powder coating uses solvent-free powder coating, there is no danger of environmental problems and disasters caused by solvents as in the coating method using solvent-based coating, and it occurs in the case of water-soluble coating. There is no wastewater treatment problem, and furthermore, it is possible to collect and reuse the oversprayed paint, so that the loss of the paint can be extremely reduced, so that it is widely used in various coating fields. It has become to.
[0003]
In addition, since it is possible to automate by a complete circulation system with a combination of a recovery device and a coating machine, it is said that efficient coating is possible including that a skilled technician is not required for the coating operation. In powder coating, a coating film is formed on an object to be coated by a method such as electrostatic spray coating or immersion coating in a fluidized bed and baked.
[0004]
However, the conventional powder coating has a drawback that a glossy and smooth coating film cannot be formed and the appearance of the coating film is poor. That is, in the process of forming a powder coating, the powder applied to the object to be coated forms a film through heat melting and subsequent curing. Since the curing proceeds before and after the melt flow at that time, the leveling becomes insufficient, and the appearance of the coating film tends to deteriorate. As a solution, it is necessary to thicken the coating, raise the baking temperature or extend the temperature holding time to sufficiently melt the resin, but completely eliminate the slight irregularities due to the shape of the powder paint particles. It is difficult. In particular, there is a problem that the unevenness is more conspicuous in the coating of a thin film, and the appearance of the coating film is further deteriorated.
[0005]
There is a strong demand for improvement in appearance, and in order to meet this demand, it is necessary to lower the melt viscosity of the resin. For the purpose of lowering the melt viscosity, methods such as lowering the glass transition temperature of the resin and lowering the molecular weight have been proposed, but when the melt viscosity is lowered to achieve a highly smooth coating film with powder, In some cases, sagging occurs during baking, making it impossible to obtain a high-appearance coating film, and also reduces coating workability. Thickening is effective as a method of improving the smoothness of the coating film, but when combined with the resin having a reduced melt viscosity, the sagging phenomenon at the time of baking becomes more remarkable.
[0006]
As a technique for improving such a defect and obtaining a smooth coating film, for example, JP-A-2001-33750 discloses a liquid resin dissolved in a solvent in addition to a liquid resin in addition to a particulate resin component of a powder coating material. Although a coating composition containing the components is disclosed, in addition to the increase in the cost of the coating material, the characteristics of the powder coating that is solvent-free are eliminated, and a problem also arises in equipment cost and solvent recovery cost. . Japanese Patent Application Laid-Open No. 8-41384 discloses that as a powder coating material having excellent transportability and forming a coating film having a high appearance, the volume average particle diameter of the coating film forming resin is set to 20 to 50 μm, and the particle size distribution standard deviation is also set. It is disclosed that a powder coating having a particle size of 20 μm or less is used. However, in order to obtain a powder coating material having a controlled particle size distribution in this way, a classification operation is required as exemplified in the same gazette, and it is inevitable that the production cost increases. The same publication also discloses, as a hybrid powder coating, a powder coating in which a resin having a low glass transition point is coated with a resin having a high glass transition point, and a powder coating having the particle size distribution is used. And the operation becomes complicated, which further increases the cost.
[0007]
[Problems to be solved by the invention]
The present invention solves the above-mentioned disadvantages of the prior art and provides a powder coating composition capable of providing a powder coating composition that forms a coating film having a high appearance, and a powder coating composition containing the filler. To provide.
[0008]
[Means for Solving the Problems]
The present inventors have conducted intensive studies to solve the above problems, and as a result, it has been found that a filler made of calcium carbonate having specific powder physical properties solves the above-mentioned conventional disadvantages as described above and provides a powder having a high appearance coating film. The present inventors have found that a body paint can be provided, and have completed the present invention.
[0009]
The first aspect of the present invention is that the BET specific surface area by the nitrogen adsorption method is 2 to 15 m. 2 / G of calcium carbonate. (Claim 1)
[0010]
In a preferred embodiment, the filler for powder coating material according to claim 1, wherein the calcium carbonate has an average particle size of 0.5 to 15 µm (claim 2).
[0011]
In a preferred embodiment, calcium carbonate is a saturated fatty acid, unsaturated fatty acid, aliphatic carboxylic acid, resin acid, (co) polymer of unsaturated carboxylic acid, alkali metal salt thereof, alkaline earth metal salt thereof, surfactant The filler for powder coating material according to claim 1 or 2, which is surface-treated with at least one selected from silane coupling agents (claim 3).
[0012]
In a preferred embodiment, the surface treatment rate is 0.05 to 0.50% by weight / m 2 per unit BET specific surface area of calcium carbonate. 2 The filler for powder coating material according to any one of claims 1 to 3, wherein the filler is (claim 4).
[0013]
A second aspect of the present invention is a powder coating composition comprising a filler for powder coating according to any one of claims 1 to 4 mixed with a powder coating resin. Item 5).
[0014]
In a preferred embodiment, the powder coating composition according to claim 5, wherein the powder coating resin is a thermosetting resin (claim 6).
[0015]
In a preferred embodiment, the powder coating composition according to claim 6, wherein the thermosetting resin comprises at least one selected from a polyester resin, an epoxy resin, an epoxy-polyester resin, a fluororesin, and an acrylic resin (claim 7). .
[0016]
As a preferred embodiment, the powder coating composition according to any one of claims 5 to 7, wherein the amount of the filler for the powder coating composition is 1 to 75 parts by weight based on 100 parts by weight of the powder coating resin. (Claim 8).
[0017]
BEST MODE FOR CARRYING OUT THE INVENTION
The filler for powder coating of the present invention has a BET specific surface area of 2 to 15 m by a nitrogen adsorption method. 2 / G of calcium carbonate.
[0018]
Calcium carbonate is generally classified into two types: heavy calcium carbonate, which is mechanically pulverized from limestone and classified into various grades by classifying the calcium carbonate, and synthetic calcium carbonate, which is prepared by a chemical method. Separated. Furthermore, (1) the limestone is prepared by reacting quicklime obtained by calcining limestone at a high temperature with water to adjust lime milk, and then conduct carbon dioxide gas generated during limestone calcination into lime milk to synthesize calcium carbonate. There are three types: a carbon dioxide compounding process, (2) a lime soda process for reacting sodium carbonate with lime milk, and (3) a solution method for reacting soluble calcium with soluble carbonate.
[0019]
The calcium carbonate constituting the filler of the present invention is not particularly limited, but the above-mentioned heavy calcium carbonate may have a reduced particle size distribution due to its production method because the particle size distribution is broad. Therefore, it is desirable to use calcium carbonate having a certain degree of fineness as a desired particle size distribution by special classification (classification is repeated many times).
[0020]
Regarding synthetic calcium carbonate, the lime soda process of reacting sodium carbonate with lime milk of the above-mentioned (2) and the solution method of reacting soluble calcium with a soluble carbonate of (3) are by-products due to the characteristics of the reaction. NaCl or the like is generated, and the cost for removing the NaCl or the like increases, which is not preferable in some cases.
[0021]
On the other hand, the carbon dioxide compounding process of the above (1) is generally preferable from an economic viewpoint, but synthetic calcium carbonate produced by using the carbon dioxide compounding process has a relatively uniform primary particle shape and is usually used. The primary particles are aggregated or aggregated to form secondary particles (aggregate particles of primary particles). As the calcium carbonate constituting the filler of the present invention, synthetic calcium carbonate (colloidal calcium carbonate) having a uniform primary particle diameter is particularly preferable.
[0022]
The BET specific surface area of the calcium carbonate used in the present invention is 2 to 15 m 2 / G, preferably 3 to 13 m 2 / G, more preferably 4 to 10 m 2 / G. BET specific surface area of calcium carbonate is 2m 2 If it is less than / g, the primary particle diameter of the extender itself becomes large, and when the powder coating is used to form a coating film, the smoothness of the coating film surface is impaired, and the appearance, particularly gloss, is impaired. On the other hand, 15m 2 / G, the primary particle size of the calcium carbonate becomes small, the cohesiveness becomes strong, and the calcium carbonate is not sufficiently dispersed when blended with the resin, or absorbs the resin or the like more than necessary, and heat-melts the powder coating. The leveling at the time is deteriorated, and the appearance of the finished coating film is impaired.
[0023]
In order for a coating film obtained using a powder coating material to have an excellent appearance (gloss), the coating material is different from a normal coating material, and it is considered that the aggregation energy of the coating powder causes a decrease in physical properties. The smaller the primary particle diameter of the calcium carbonate compounded therein, the higher the BET specific surface area. It is considered that the higher the BET specific surface area is, the larger the cohesive energy of the coating powder is and the poorer the appearance is. On the other hand, if the BET specific surface area is low (primary particles are large below a certain level), it is considered that the smoothness is impaired and the appearance, particularly the gloss, is impaired.
[0024]
In addition, the agglomeration of the powder coating is affected by the particle diameter of the powder particles, and the smaller the particle size, the stronger the cohesive force. Therefore, in order to prevent the agglomeration, the powder coating contains a chemical agent such as a surface conditioner, unlike the ordinary solvent-based coating. When calcium carbonate having a relatively large BET specific surface area is mixed therein, the calcium carbonate adsorbs a drug or the like and does not sufficiently perform functions such as surface adjustment, and the paint powder itself agglomerates. It is considered that a coating film having a high appearance cannot be obtained. Therefore, the BET specific surface area of calcium carbonate needs to be adjusted to the above range.
[0025]
In addition, the calcium carbonate used in the present invention usually has primary particles aggregated or aggregated to form secondary particles (aggregate particles of primary particles). It is preferable to satisfy the average particle size (the particle size configuration as secondary particles), whereby the re-aggregation of the coating powder can be prevented, and an excellent appearance can be obtained when the powder coating is applied.
[0026]
That is, the average particle diameter of the calcium carbonate used in the present invention is preferably 0.5 to 15 μm, more preferably 0.75 to 12 μm, and further preferably 1.0 to 10 μm. If the average particle size is less than 0.5 μm, the cohesiveness is so strong that sufficient dispersion cannot be obtained when compounding the resin, or the resin resin or additives are adsorbed more than necessary, and the powder coating is heated and melted. It is not preferable because the leveling at the time is deteriorated and the appearance of the finished coating film may be impaired. On the other hand, when the thickness exceeds 15 μm, when the powder coating is used to form a coating film, the smoothness of the coating film surface is impaired, and the appearance, particularly gloss, may be impaired, which is not preferable.
[0027]
The average particle diameter was measured under the following conditions.
Particle size distribution measurement conditions: The following ingredients (I) and (II) were weighed into a 140 ml mayonnaise bottle, stirred with a stainless steel spoon until visually dispersed, diluted with the ingredient (III), and then ultrasonically dispersed. The pre-dispersed sample was used as a sample, and the measurement was performed using a laser diffraction type particle size distribution meter (manufactured by Shimadzu Corporation: SALD-2000).
(I) Neutral detergent (5 times diluted with water) 2.0 g
(II) Calcium carbonate sample 0.4 g
(III) 40 g of water
In addition, after adjusting with the above-mentioned composition as a pretreatment, it was preliminarily dispersed under a constant condition of 100 μA for 60 seconds using an ultrasonic dispersing machine US-300T (manufactured by Nippon Seiki Seisakusho). The neutral detergent is not particularly limited and is a general commercial product without any problem. In the present invention, mama lemon (manufactured by Lion Corporation) was used.
[0028]
The calcium carbonate used in the present invention may be, for example, a method of passing a carbon dioxide-containing gas (hereinafter referred to as carbon dioxide gas) to an aqueous suspension of calcium hydroxide (hereinafter referred to as lime milk), or a method of introducing lime milk or calcium hydroxide into carbon dioxide gas. It is manufactured by a known method such as a method of spraying a mixed solution of urea and precipitated calcium carbonate. It is preferable to disperse the calcium carbonate particles as much as possible. For example, as a method, the carbonation reaction is stopped at a pH of 7.5 to 10.0 of the reaction system, the mixture is stirred, and the calcium carbonate particles remain in the calcium carbonate. A method in which the pH of the system is controlled at 9.0 to 12.0 for 5 hours or more by eluting the alkali component to be added, and adding or conducting milk of lime and carbon dioxide as needed in the system.
[0029]
In order to obtain fine heavy calcium carbonate, limestone produced naturally is pulverized by a dry method or a wet method to adjust to fine particles having an average particle diameter of 0.4 to 1.0 μm. In the case of the dry type, it may be pulverized by a micron mill, a vibrating ball mill or the like, and then classified by an air classifier. In the case of the wet type, it may be pulverized by a continuous wet disperser such as a ball mill or a tower mill, and is not particularly limited.
[0030]
The calcium carbonate used in the present invention is preferably subjected to a surface treatment for improving the surface activity and improving the affinity with the powder coating resin.
[0031]
Examples of surface treatment agents include saturated fatty acids, unsaturated fatty acids, alicyclic carboxylic acids, resin acids and their alkali metal salts, alkaline earth metal salts, surfactants, silane coupling agents, and polymer (co) polymers. Products, their alkali metal salts, their alkaline earth metal salts, and the like. Specifically, saturated fatty acids such as caprylic acid, lauric acid, myristic acid, palmitic acid, stearic acid, and aragic acid; unsaturated fatty acids such as oleic acid, elaidic acid, linoleic acid, and ricileic acid; and alicyclic rings such as naphthenic acid Resin acids such as aromatic carboxylic acids, abietic acid, pimaric acid, parastolic acid, and neoabietic acid; and alkali metals, alkaline earth metals, NH 3 , Al, Zn or the like, or a partially neutralized salt. In addition, dodecylbenzenesulfonic acid, dialkyl sulfosuccinate and sulfonic acid type represented by Na salt thereof, sulfate ester type represented by sodium dodecyl sulfate, sodium monolauryl phosphate, dodecyl polysulfate Anionic surfactants such as phosphate esters represented by oxyethylene and salts thereof, amine salts represented by stearylamine hydrochloride, and quaternary ammonium represented by stearyltrimethylammonium chloride Cationic surfactants such as salt type, ester type typified by glycerin monostearate, ether type typified by polyoxyethylene nonyl phenyl ether, typified by polyethylene glycol oleate Beauty treatment Non-ionic surfactants such as alkanolamides represented by ether type and lauric acid diethanolamide, and silane coupling agents such as vinyl silane, amino silane, epoxy silane, chloroalkyl silane, and methyl triethoxy silane are exemplified. Can be Further, acrylic acid, itaconic acid, unsaturated monocarboxylic acid such as maleic acid, a polymer of a monomer composed of an unsaturated dicarboxylic acid and the like or an alkali metal of a copolymer with a monomer copolymerizable therewith, Alkaline earth metal, NH 3 , Al, Zn or the like, or a completely neutralized salt. These surface treatment agents may be treated alone or in combination of two or more. Among these, alkali metal salts of saturated fatty acids and alkali metal salts of resin acids are preferred because they have good reactivity with calcium carbonate and are easily available industrially.
[0032]
The treatment amount of the surface treatment agent may be appropriately selected depending on the kind of the powder coating resin to be used, as long as the surface treatment of the calcium carbonate particles can be uniformly performed. It is preferably from 0.5 to 0.50% by weight, more preferably from 0.07 to 0.40% by weight. If the amount is less than 0.05% by weight, the treatment amount per unit BET specific surface area is reduced, and the effect of the surface treatment cannot be sufficiently exhibited, which may be undesirable. If the content exceeds 0.5% by weight, the amount of treatment per unit BET specific surface increases, and the excessive surface treatment agent adversely affects the physical properties of the coating resin, or the excessive surface treatment agent melts during baking during film formation. In some cases, the coating film becomes cloudy, which is not preferable.
[0033]
The method of obtaining the surface-treated calcium carbonate as a powder may be a conventional method. For example, it is added to a calcium carbonate slurry having an average particle diameter of 0.01 to 1.0 μm obtained by the above-described production method, and stirred. After the surface treatment agent is adsorbed on the calcium carbonate particles by mixing more uniformly, the mixture can be obtained by dehydrating, drying and pulverizing with a filter press or the like. Further, the calcium carbonate slurry after completion of carbonation is once dehydrated, the surface treating agent is added to a calcium carbonate press cake, and the mixture is vigorously stirred, and then dried and powdered with a spray drier or the like. Further, as a method of firmly fixing the calcium carbonate on the surface of the calcium carbonate, it is also effective to disperse the calcium carbonate slurry to which the surface treating agent has been added using a continuous wet disperser such as a sand grinder before drying.
[0034]
The powder coating composition of the present invention is obtained by blending the filler for powder coating of the present invention obtained as described above with a powder coating resin. The powder coating resin is not particularly limited, and those commonly used in the field of powder coating can be used. Examples of such a resin include a thermoplastic resin and a thermosetting resin. it can. The thermoplastic resin is not particularly limited, but particularly, a vinyl resin such as a polyvinyl chloride resin, a polyethylene resin, a polyamide resin, a fluororesin, or the like can be suitably used. The thermosetting resin is not particularly limited, but in particular, an epoxy resin, an epoxy-polyester resin, an acrylic resin, a fluororesin, a polyester resin, or the like can be suitably used. When a thermosetting resin is used as the coating resin, the powder coating composition of the present invention preferably contains a curing agent and a curing accelerator.
[0035]
The compounding amount of the filler for powder coating of the present invention is 1 to 75 parts by weight, preferably 5 to 70 parts by weight, more preferably 10 to 50 parts by weight based on 100 parts by weight of the powder coating resin. If the compounding amount of the filler for powder coating is less than 1 part by weight, a sufficient effect cannot be obtained. It is not preferable because the workability is deteriorated due to too high or the coating film itself may not be formed.
[0036]
In the powder coating composition of the present invention, when it is necessary to form a coating film having good weather resistance, it is necessary to form an acrylic resin system, and to form a coating film having good coating properties such as impact resistance. In some cases, it is preferable to use a polyester resin, and when it is necessary to form a coating film having good corrosion resistance, it is preferable to use an epoxy resin. If necessary, two or more resins may be used in combination, such as coating a resin having a low glass transition point with a resin having a high glass transition point.
[0037]
In the present invention, when using an epoxy resin as the powder coating resin, if necessary, for example, phthalic anhydride, an amine compound, an imidazole compound, a curing agent such as dicyandiamide, a curing accelerator can be used, Further, another resin such as an acrylic resin can be used in combination. When using a thermosetting acrylic resin as the powder coating resin, if necessary, for example, use another resin such as an epoxy resin or a melamine resin, or use a curing agent such as a polyvalent carboxylic acid or a blocked isocyanate compound. can do.
[0038]
In the present invention, when using a thermosetting polyester resin as the powder coating resin, if necessary, for example, other resins such as melamine resin, epoxy resin, polybasic acid, blocked isocyanate compound, triglycidyl isocyanate A curing agent such as nurate can be used.
[0039]
The content of the curing agent is preferably 5 to 80 parts by weight per 100 parts by weight of the thermosetting resin used as the powder coating resin. If the amount is less than 5 parts by weight, the curing will be insufficient, and if it exceeds 80 parts by weight, the curing will proceed too much and the physical properties of the coating film will be reduced. The content of the curing accelerator is preferably from 0.1 to 5 parts by weight per 100 parts by weight of the thermosetting resin used as the powder coating resin. If the amount is less than 0.1 part by weight, the curing is insufficient, and if it exceeds 5 parts by weight, the curing is excessively advanced, and the physical properties of the coating film tend to decrease.
[0040]
The powder coating composition of the present invention may contain a pigment and other additives as necessary. Examples of the other additives include other resins, curing agents, curing accelerators or curing catalysts, surface conditioners, plasticizers, ultraviolet absorbers, antioxidants, anti-penetrating agents, pigment dispersants, and the like. . The pigment is not particularly limited, and among them, titanium dioxide, red iron oxide, yellow iron oxide, carbon black, phthalocyanine blue, phthalocyanine green, quinacridone red pigment, and the like can be preferably used. These may be used alone or in combination of two or more as necessary.
[0041]
The content of the pigment is preferably 1 to 60 parts by weight based on 100 parts by weight of the powder coating composition. If the content is less than 1 part by weight, the effect of the pigment such as coloring cannot be obtained, and if it exceeds 60 parts by weight, a high-appearance coating film cannot be obtained. The pigment and other additives may be contained in the powder coating particles together with the powder coating resin or the like, or may be added as particles separate from the powder coating resin.
[0042]
The particles of the powder coating resin can be directly produced, for example, by a method such as emulsion polymerization or suspension polymerization. Alternatively, the resin can be produced by producing a resin by solution polymerization, bulk polymerization, or the like, and pulverizing and classifying the resin.
[0043]
The method for producing the powder coating composition of the present invention is not particularly limited, and it can be carried out by a method generally used in the field of powder coating production. For example, the above-mentioned powder coating resin, and, if necessary, a pigment and other additives are uniformly mixed by a mixer such as a Henschel mixer, a super mixer, a ball mill, and a Banbury mixer, and then the obtained product is obtained. The mixture thus obtained is melt-kneaded with a kneader such as an extruder or a hot roll, components other than the resin are uniformly dispersed in the molten powder coating resin, and the resulting mixture is formed into pellets. The obtained pellets are pulverized by an impact pulverizer such as a hammer mill or an air current pulverizer such as a jet mill, and then classified to obtain the powder coating composition of the present invention.
[0044]
The classification is carried out by using a 170 mesh, preferably 200 mesh Tyler standard sieve, a fluid separator such as a dispersion separator for separating and removing particles larger than 90 μm, preferably 80 μm, a micron separator, and a particle smaller than 1 μm. The separation and removal can be performed using a fluid classifier such as a cyclone, a dispersion separator, or a micron separator.
[0045]
As a method for producing the powder coating composition of the present invention, in addition to the above-described methods, for example, raw materials are mixed in a solvent, and the obtained mixture is dried, finely pulverized, or powdered by a spray dry method. It is also possible to adopt a method of doing so. The obtained powder can be subjected to the above-mentioned pulverization and classification as needed.
[0046]
When such a powder coating material is used, pellets in which a pigment and various additives are uniformly dispersed in a resin component can be obtained. Therefore, the powder coating obtained by pulverizing the pellets contains various raw material components in each particle. Are almost equally included. For this reason, in the coating film forming step, for example, the curing reaction of the resin is likely to occur uniformly, so that a coating film having better appearance such as smoothness can be formed.
[0047]
The application target of the powder coating composition of the present invention is not particularly limited, and includes, for example, steel plates for automobiles, home appliances, building materials, miscellaneous goods, zinc phosphate treated steel plates, aluminum or aluminum alloy materials, and the like. be able to. As a coating method of the powder coating composition of the present invention, for example, the powder coating composition of the present invention is deposited to a desired thickness on the surface of the object to be coated by a known method such as an electrostatic spraying method and a fluid immersion method. And then baking. When a thermosetting resin is used as the resin component, a cured coating film is formed.
[0048]
【Example】
Hereinafter, the present invention will be described in more detail by way of examples, but the present invention is not limited to these examples.
[0049]
Example 1
Lime milk having a specific gravity of 1.06 was adjusted to 15 ° C., and carbon dioxide gas (30% / min. 2 ) Was conducted to carry out a carbonation reaction, and after the carbonation reaction was stopped when the pH of the system reached 8.5, the system was stirred at 50 ° C. for 24 hours under the conditions of 10 to 11 to obtain a system. The average primary particle diameter of the aggregate particles is extremely small due to 0.10 μm, and the BET specific surface area is 11 m. 2 / G of calcium carbonate was obtained. Lime milk having a specific gravity of 1.06 and a temperature of 16 ° C. is added to the calcium carbonate slurry, and 3 liters / minute of carbon dioxide gas (of which 25% CO 2 is contained) per kg of calcium hydroxide. 2 ) Was conducted to carry out a carbonation reaction until the pH of the system reached 8.5. Lime milk adjusted in the same manner as described above was further added to the obtained calcium carbonate slurry, and a calcium carbonate slurry was obtained by the same operation. By repeating this operation several times, the BET specific surface area with a very small amount of aggregated particles is 6.5 m. 2 / G, and a calcium carbonate slurry having an average particle size of 3.17 µm. This calcium carbonate slurry was treated with a solution of potassium abietate at a concentration of 10% with respect to the solid content of calcium carbonate at a treatment rate of 0.20% / m 2. 2 After performing surface treatment, the mixture was dehydrated with a filter press, dried and crushed to obtain a filler for powder coating.
[0050]
Example 2
Lime milk having a specific gravity of 1.06 was adjusted to 15 ° C., and carbon dioxide gas (30% / min. 2 ) Was conducted to carry out a carbonation reaction, and when the pH of the system was 8.5, the carbonation reaction was stopped. Then, the system was stirred at 50 ° C. for 24 hours under the conditions of 10 to 11 and again. The pH of the system was adjusted to 6.8 by passing carbon dioxide gas. As a result, the average primary particle diameter of the aggregate particles was very small, 0.10 μm, and the BET specific surface area was 11 m. 2 / G, an aqueous slurry of calcium carbonate having an average particle diameter of 4 µm was obtained. This calcium carbonate slurry was treated with a solution of potassium abietate at a concentration of 10% with respect to the solid content of calcium carbonate at a treatment rate of 0.25% / m 2. 2 After performing surface treatment, the mixture was dehydrated with a filter press, dried and crushed to obtain a filler for powder coating.
[0051]
Example 3
Lime milk having a specific gravity of 1.06 was adjusted to 15 ° C., and carbon dioxide gas (30% / min. 2 ) Was conducted to carry out a carbonation reaction, and when the pH of the system was 8.5, the carbonation reaction was stopped. Then, the system was stirred at 50 ° C for 15 hours under the conditions of 10 to 11 to obtain a slurry system. When the viscosity reached 2,300 cp, carbon dioxide gas was passed again to adjust the pH of the system to 6.8. Thereby, the average primary particle diameter of the aggregate particles is extremely small, 0.07 μm, and the BET specific surface area is 14 m. 2 / G, an aqueous slurry of calcium carbonate having an average particle diameter of 4 µm was obtained. The calcium carbonate slurry was treated with a 10% solution of sodium stearate at a treatment rate of 0.25% / m 2 based on the solid content of calcium carbonate. 2 After performing surface treatment, the mixture was dehydrated with a filter press, dried and crushed to obtain a filler for powder coating.
[0052]
Example 4
After limestone produced naturally was pulverized by a micron mill, classification was repeated by an air classifier to obtain particles having an average particle diameter of 2.0 μm. Thereafter, using a Henschel mixer, potassium abietic acid was treated at a treatment rate of 0.25% / m with respect to the solid content of calcium carbonate. 2 To obtain a powder coating filler.
[0053]
Example 5
In Example 1, the BET specific surface area was 6.5 m by changing the carbon dioxide gas flow rate from 3 L / min to 10 L / min. 2 / G, calcium carbonate having an average particle size of 6.5 μm, and then subjected to the same surface treatment as in Example 1 to obtain a filler for powder coating.
[0054]
Example 6
In Example 1, the BET specific surface area was 5.2 m by changing the flow rate of carbon dioxide gas from 3 L / min to 15 L / min. 2 / G, calcium carbonate having an average particle size of 12.5 μm, and the same operation was performed except that the surface treatment agent was changed to sodium stearate, to obtain a filler for powder coating.
[0055]
Example 7
In Example 1, the treatment rate was changed to 0.08% / m by changing the surface treatment agent to sodium stearate. 2 The same operation was performed except for changing to the above, to obtain a filler for powder coating.
[0056]
Example 8
In Example 1, the treatment rate was changed to 0.04% / m by changing the surface treatment agent to sodium stearate. 2 The same operation was performed except for changing to the above, to obtain a filler for powder coating.
[0057]
Example 9
After limestone produced in nature is pulverized with a micron mill, classification is repeated with an air classifier, and the BET specific surface area is 5.2 m. 2 / G, having a mean particle size of 3.7 μm.
[0058]
Comparative Example 1
A BET specific surface area of 18 m was obtained in the same manner as in Example 1, except that the aging time after completion of carbonation was changed to 10 hours. 2 / G, an average particle diameter of 2 μm was obtained. Then, potassium abietic acid was treated in the same manner as in Example 1 with respect to the solid content of calcium carbonate at a treatment rate of 0.2% / m 2. 2 To obtain a powder coating filler.
[0059]
Comparative Example 2
After limestone produced in nature is crushed with a micron mill, classification is repeated with an air classifier, and the BET specific surface area is 2.5 m. 2 / G, calcium carbonate particles having an average particle size of 25 μm. Thereafter, using a Henschel mixer, potassium abietic acid was treated at a treatment rate of 0.25% / m with respect to the solid content of calcium carbonate. 2 To obtain a powder coating filler.
[0060]
Table 1 shows the properties of the powder coating fillers obtained in Examples 1 to 9 and Comparative Examples 1 and 2.
[0061]
[Table 1]
Figure 2004010735
[0062]
Examples 10 to 22, Comparative Examples 3 to 5
Using the fillers for powder coatings obtained in Examples 1 to 9 and Comparative Examples 1 and 2, powder coating compositions were prepared in the following manner, and their coating properties were tested.
[0063]
Figure 2004010735
[0064]
Figure 2004010735
[0065]
Figure 2004010735
[0066]
The above components were mixed as a raw material in a super mixer (manufactured by Nippon Spindle Manufacturing Co., Ltd.) for about 3 minutes, and melt-kneaded at about 100 ° C. using a coneder (manufactured by Bus). After cooling at room temperature, the mixture was coarsely pulverized and then pulverized with an atomizer (manufactured by Fuji Paudal), and classified with a 150-mesh sieve to obtain a powder coating having a volume average particle diameter of 35 μm.
[0067]
Each of the powder coatings produced by the above method was applied to a 200 × 100 × 0.8 mm zinc phosphate treated steel sheet by electrostatic spraying with a corona charging type coating gun to a film thickness of about 60 μm. After baking under each condition of 180 ° C. × 20 min and 200 ° C. × 20 min, it was allowed to cool to room temperature. The coating film performance was evaluated by the following method.
[0068]
<Appearance evaluation>
◎: Smooth coating state with little unevenness.
:: Smooth coating film state with some unevenness.
Δ: Slight irregularities and slight bumps.
X: There are irregularities, and the smoothness is slightly inferior.
XX: There are bumps and the like, poor in smoothness, and accumulation at the lower edge portion of the test plate is observed.
[0069]
<Pellet flow value>
Using a tableting machine, each powder coating was 300 kg / cm 2 Under pressure to form a disk-shaped pellet having a diameter of 50 mm. As shown in FIG. 1, the pellet 1 was fixed to a metal plate of 200 × 100 mm with a double-sided tape, and the metal plate 2 was baked at 180 ° C. for 20 minutes while being suspended vertically, and the pellet 1 was flowed. Paint length 3 was measured. The above test was performed three times, and the average value was used as the evaluation value.
[0070]
<Gloss value>
As described above, any five places were selected from the coating surface of each test plate baked at 180 ° C. × 20 min and 200 ° C. × 20 min, and the gloss was measured at 60 ° by a gloss meter (manufactured by Nippon Denshoku Co., Ltd.). , 20 ° gloss was measured, and the average value was used as the evaluation value.
[0071]
[Table 2]
Figure 2004010735
[0072]
【The invention's effect】
As described above, the filler for powder coating of the present invention can provide a powder coating composition that forms a coating film having an excellent appearance.
[Brief description of the drawings]
FIG. 1 is an explanatory diagram showing a method of measuring a pellet flow value.
[Explanation of symbols]
1 pellet
2 Metal plate
3 Paint flow length

Claims (8)

窒素吸着法によるBET比表面積が2〜15m/gの炭酸カルシウムからなることを特徴とする粉体塗料用充填剤。A filler for powder coatings, comprising calcium carbonate having a BET specific surface area of 2 to 15 m 2 / g by a nitrogen adsorption method. 炭酸カルシウムの平均粒子径が0.5〜15μmである請求項1記載の粉体塗料用充填剤。The filler for powder coating materials according to claim 1, wherein the average particle size of the calcium carbonate is 0.5 to 15 µm. 炭酸カルシウムが飽和脂肪酸、不飽和脂肪酸、脂肪族カルボン酸、樹脂酸、不飽和カルボン酸の(共)重合物、それらのアルカリ金属塩、それらのアルカリ土類金属塩、界面活性剤、シランカップリング剤から選ばれる少なくとも1種で表面処理されている請求項1又は2記載の粉体塗料用充填剤。Calcium carbonate is a saturated fatty acid, unsaturated fatty acid, aliphatic carboxylic acid, resin acid, (co) polymer of unsaturated carboxylic acid, their alkali metal salts, their alkaline earth metal salts, surfactant, silane coupling The filler for powder coating according to claim 1 or 2, which is surface-treated with at least one selected from agents. 表面処理率が炭酸カルシウムの単位BET比表面積当たり0.05〜0.50重量%/mである請求項1〜3のいずれか1項に記載の粉体塗料用充填剤。Powder coating filler according to any one of claims 1 to 3 surface treatment ratio is the unit BET specific surface area per 0.05-0.50 wt% / m 2 of calcium carbonate. 請求項1〜4のいずれか1項に記載の粉体塗料用充填剤を粉体塗料樹脂に配合してなることを特徴とする粉体塗料組成物。A powder coating composition comprising the powder coating resin according to any one of claims 1 to 4 mixed with a powder coating resin. 粉体塗料樹脂が熱硬化性樹脂である請求項5記載の粉体塗料組成物。The powder coating composition according to claim 5, wherein the powder coating resin is a thermosetting resin. 熱硬化性樹脂がポリエステル樹脂、エポキシ樹脂、エポキシ−ポリエステル樹脂、フッ素樹脂、アクリル樹脂から選ばれる少なくとも1種からなる請求項6記載の粉体塗料組成物。The powder coating composition according to claim 6, wherein the thermosetting resin comprises at least one selected from a polyester resin, an epoxy resin, an epoxy-polyester resin, a fluororesin, and an acrylic resin. 粉体塗料用充填剤の配合量が粉体塗料樹脂100重量部に対し1〜75重量部である請求項5〜7のいずれか1項に記載の粉体塗料組成物。The powder coating composition according to any one of claims 5 to 7, wherein the compounding amount of the powder coating filler is 1 to 75 parts by weight based on 100 parts by weight of the powder coating resin.
JP2002165255A 2002-06-06 2002-06-06 Filler for powder coating and powder coating composition comprising the same Pending JP2004010735A (en)

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006064821A1 (en) * 2004-12-13 2006-06-22 Shiseido Co., Ltd. Modified powder and cosmetic composition using same
WO2007029869A1 (en) * 2005-09-06 2007-03-15 Maruo Calcium Company Limited Filler for powder coating material and powder coating composition containing the same
KR100750615B1 (en) 2005-12-30 2007-08-20 삼화페인트공업주식회사 Low noise epoxy flooring coating composition
US7759421B2 (en) * 2004-04-21 2010-07-20 Achilles Corporation Heat-stable soft resinous sheet articles and compositions therefor
CN104403371A (en) * 2014-11-28 2015-03-11 黄国新 Method for preparing silicane-modified heavy calcium carbonate powder
JPWO2013168600A1 (en) * 2012-05-08 2016-01-07 丸尾カルシウム株式会社 Surface treated calcium carbonate filler and curable resin composition containing the filler
US10197856B2 (en) 2015-04-03 2019-02-05 Sharp Kabushiki Kaisha Optical modulator and display device
CN111423786A (en) * 2020-04-26 2020-07-17 常州市碳索新材料科技有限公司 Graphene modified powder coating for subway tunnel embedded groove and preparation method thereof
WO2022129201A1 (en) 2020-12-18 2022-06-23 Eckart Gmbh Platelet-like matting agent for powder coating and powder coatings
CN114672069A (en) * 2022-04-01 2022-06-28 科顺防水科技股份有限公司 Modified cast stone/porous carbon composite material, preparation method thereof, epoxy resin-based composite material and epoxy floor coating

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7759421B2 (en) * 2004-04-21 2010-07-20 Achilles Corporation Heat-stable soft resinous sheet articles and compositions therefor
JPWO2006064821A1 (en) * 2004-12-13 2008-06-12 株式会社資生堂 Modified powder and cosmetics using the same
WO2006064821A1 (en) * 2004-12-13 2006-06-22 Shiseido Co., Ltd. Modified powder and cosmetic composition using same
US8138253B2 (en) 2005-09-06 2012-03-20 Maruo Calcium Company Limited Filler for powder coating material and powder coating composition containing the same
JP4897687B2 (en) * 2005-09-06 2012-03-14 丸尾カルシウム株式会社 Powder coating filler and powder coating composition comprising the same
WO2007029869A1 (en) * 2005-09-06 2007-03-15 Maruo Calcium Company Limited Filler for powder coating material and powder coating composition containing the same
KR101272048B1 (en) 2005-09-06 2013-06-07 마루오 칼슘 가부시키가이샤 Filler for powder coating material and powder coating composition containing the same
KR100750615B1 (en) 2005-12-30 2007-08-20 삼화페인트공업주식회사 Low noise epoxy flooring coating composition
JPWO2013168600A1 (en) * 2012-05-08 2016-01-07 丸尾カルシウム株式会社 Surface treated calcium carbonate filler and curable resin composition containing the filler
CN104403371A (en) * 2014-11-28 2015-03-11 黄国新 Method for preparing silicane-modified heavy calcium carbonate powder
US10197856B2 (en) 2015-04-03 2019-02-05 Sharp Kabushiki Kaisha Optical modulator and display device
CN111423786A (en) * 2020-04-26 2020-07-17 常州市碳索新材料科技有限公司 Graphene modified powder coating for subway tunnel embedded groove and preparation method thereof
WO2022129201A1 (en) 2020-12-18 2022-06-23 Eckart Gmbh Platelet-like matting agent for powder coating and powder coatings
CN114672069A (en) * 2022-04-01 2022-06-28 科顺防水科技股份有限公司 Modified cast stone/porous carbon composite material, preparation method thereof, epoxy resin-based composite material and epoxy floor coating

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