JPH0372714B2 - - Google Patents

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Publication number
JPH0372714B2
JPH0372714B2 JP24407587A JP24407587A JPH0372714B2 JP H0372714 B2 JPH0372714 B2 JP H0372714B2 JP 24407587 A JP24407587 A JP 24407587A JP 24407587 A JP24407587 A JP 24407587A JP H0372714 B2 JPH0372714 B2 JP H0372714B2
Authority
JP
Japan
Prior art keywords
chromate
coating
layer
treatment
resin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP24407587A
Other languages
Japanese (ja)
Other versions
JPS6487783A (en
Inventor
Yukinobu Higuchi
Kenichi Asakawa
Hirobumi Nakano
Keizo Ooshiba
Ryusuke Inoe
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
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Nippon Steel Corp
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Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP24407587A priority Critical patent/JPS6487783A/en
Publication of JPS6487783A publication Critical patent/JPS6487783A/en
Publication of JPH0372714B2 publication Critical patent/JPH0372714B2/ja
Granted legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/73Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals characterised by the process
    • C23C22/76Applying the liquid by spraying

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  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemical Treatment Of Metals (AREA)

Description

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

(産業上の利用分野) 本発明は、金属表面処理を施した鋼板に、二層
型クロメート被膜を施した耐食性及び塗装性能の
優れた金属表面処理鋼板の製造方法に関するもの
である。 ここでいう金属表面処理鋼板とは、亜鉛、及び
亜鉛合金メツキ鋼板、鉛及び鉛合金メツキ鋼板、
アルミ及びアルミ合金メツキ鋼板のように金属メ
ツキを施した鋼板である。具体的に、亜鉛メツキ
及び亜鉛合金メツキ鋼板としては、 (a) 電気メツキ、真空蒸着メツキによるメツキ
で、不可避的に不純物として混入してくる元素
を含む亜鉛メツキ鋼板 (b) Alを0.1〜0.3%、他物質としてPb、Cd、Fe、
Sb等の元素を1種又は2種以上含み、更に不
可避的不純物元素を含む、溶融亜鉛メツキ鋼板 (c) Feを5〜90%及び不可避的不純物元素を含
むFe−Zn合金めつき鋼板 (d) Niを5〜20%及び不可避的不純物元素を含
むZn−Ni合金メツキ鋼板 (e) Alを3〜60%含み、又はこれにSi、Mg、ミ
ツシユメタル或いは不可避的不純物を含むZn
−Al合金メツキ鋼板 等を挙げることができ、又、鉛メツキ、及び鉛合
金メツキ鋼板としては、 (a) 製造工程上、不可避的不純物を含む、鉛メツ
キ鋼板 (b) Snが30%以下含有され、場合によつてはSb、
Zn或いは不可避的不純物元素を含むPb−Sn合
金メツキ鋼板 等を挙げることができ、更に、アルミ、及びアル
ミ合金メツキ鋼板としては、 (a) メツキ時に不可避的に、Fe及びその他の元
素を少量含む、アルミメツキ鋼板 (b) Si、Mgの1種又は2種以上を含み、Siが12
%以下、或いはMgが5%以下であるアルミ合
金メツキ鋼板等を挙げることができる。 (従来の技術) 近時、ユーザーから、亜鉛メツキ鋼板、亜鉛系
合金メツキ鋼板等の金属表面処理鋼板に対し、外
観性、均一被覆性、耐食性及び塗装性能(塗料密
着性、塗装後耐食性等)のすぐれた処理法が強く
望まれていることから、各種のクロメート処理が
施されている。例えば、 (1) 表面処理鋼板の表面上に、有機樹脂中にクロ
ム化合物を含有せしめた水溶液を塗布し次いで
乾燥することにより被膜を形成する方法(例え
ば特開昭59−200768号)。 (2) 表面処理鋼板の表面上に、有機樹脂中にクロ
ム化合物を含有せしめた水溶液を塗布し次いで
乾燥することにより第1層の被膜を形成し、次
いで前記第1層の被膜の表面上に更に水溶性有
機樹脂を塗布する第2層の被膜を形成する方法
(例えば特開昭59−14552号)。 (3) 表面処理鋼板の表面上に、クロム化合物と無
機酸とからなる水溶液を塗布し次いで乾燥する
ことにより第1層の被膜を形成し、次いで前記
第1層の被膜の表面上に更に水溶性有機樹脂を
塗布する第2層の被膜を形成する方法(例えば
特開昭59−166678号、特開昭59−162278号、特
開昭59−162279号)。 (4) 亜鉛メツキまたは合金化亜鉛メツキ鋼板の表
面処理鋼板に、リン酸、亜鉛イオン、フツ素イ
オンを含有するクロム化合物水溶液を塗布して
第1層のクロメート被膜を施し、その上に二酸
化ケイ素と上記の各含有イオンを加えたクロム
化合物の水溶液を塗布して第2層のクロメート
被膜を形成する方法(例えば、特開昭62−
4880)。 等がある。 (発明の解決しようとする問題点) 上記(1)の方法で製造された表面処理鋼板は、塗
膜密着性および塗装後の耐食性に優れてはいる
が、無塗装での裸耐食性に劣る問題を有してい
る。即ち、上記(1)の方法で形成された被膜中には
多くの有機物が含有されるため、無塗装で腐食環
境に長期間曝された場合の有機物の官能基が水分
を吸収し、さらに水分が被膜中に侵入して裸耐食
性を劣化せしめる傾向にある。 上記(2)および(3)の方法で製造された表面処理鋼
板は、無塗装で裸耐食性および塗膜密着性に優れ
ている。しかしながら、第1層の被膜の表面上
に、第2層の被膜の水溶性有機樹脂を塗布する際
に、第1層のクロメート被膜の乾燥或いは不溶解
化反応が不十分な場合は、この被膜成分が第2層
の水溶性有機樹脂中に溶出し、水溶性有機樹脂を
ゲル化して、水溶性有機樹脂浴の浴寿命の劣化を
もたらし、また第2層の被膜性能を劣化せしめ
る。 従つて、第1層の被膜の乾燥或いは不溶解化反
応を充分に行なわしめるためにはインダクシヨン
ヒーターや赤外線ヒーターなどの乾燥装置を必要
とし、また十分な乾燥、不溶解化反応のために長
時間を要する問題もあつた。さらには、経時によ
つて、第2層の有機被膜中の有機樹脂が、第1層
被膜中のCr6+と反応して、被膜性能が劣化する問
題もあつた。 また、これらの有機樹脂或いはクロム化合物を
含有する有機樹脂の水溶液を表面処理鋼板の表面
に塗布する場合、良好な外観性能、被膜の均一被
覆性を確保するため、主としてロールコーターに
よる被覆方法を採用している。 この方法は、被膜量が1μ厚さ以上、好ましく
は3μ以上の厚い被覆層を設ける場合には、均一
被覆性に有利であるが、1μ未満の薄い被覆層を
均一に施し、外観性能、延いては耐食性能にすぐ
れた被膜を形成するのは困難である。 また、上記(4)の方法については、第1層のクロ
メート被膜の第2層形成処理浴中への溶出が長期
作業によつて生じる。したがつて第2層に性能良
好なクロメート被膜を形成するためには、第1層
被膜からの溶出イオンのコントロールを行なう必
要と第2層の処理浴の浴組成調整、管理を煩雑に
行なう必要があるなどの問題があつた。 又、特開昭52−10834号公報には、クロム化合
物、コロイダルシリカを含有する水溶液等を静電
霧化塗装機で金属の表面に付着するクロメート処
理法が公開されている。 しかし、この方法は、クロム化合物を含有する
水溶液の静電下、霧化状態で塗布する方法である
ため、霧化粒子を金属表面に効率的に付着させる
が、付着粒子間同志の間〓が存在し、クロメート
被膜の均一被覆性が劣化し、耐食性を劣化する問
題があつた。 本発明は、前記した各種クロメート処理法の性
能上の問題点、処理時の問題点を解決し、外観
性、均一被覆性、耐食性及び塗装性能のすぐれた
クロメート処理法を工業的に安定して鋼板表面に
形成することを目的としている。 (問題点を解決するための手段) 亜鉛又は亜鉛合金メツキ鋼板、アルミ又はアル
ミ合金メツキ鋼板、鉛又は鉛合金メツキ鋼板など
金属表面処理鋼板の処理外観、被膜均一性、耐食
性及び塗装性能にすぐれたクロメート二層被膜の
金属表面処理鋼板の製造方法について種々検討し
た結果、第2層のクロメート浴の構成、性状を静
電霧化粒子の均一形成に適合せしめると共に、こ
のクロメート浴を第1層のクロメート被膜を施し
た金属表面処理鋼板に静電霧化法、第2層のクロ
メート被膜を付着、形成せしめることにより、第
1層にクロメート被膜を形成するクロメート浴の
混入によつて第2層被膜形成のクロメート浴が汚
染されない事、又第2層のクロメート被膜がその
被膜量(厚さ)の如何にかかわらず所定の被膜量
に設ける事ができしかも第1層のクロメート被膜
との重畳効果によつて均一被膜性にすぐれた被膜
が得られることを知見した。 本発明はこの知見に基づいて構成したもので、
その要旨は、金属表面処理を施した鋼板にCr6+
主成分とする水溶液の電解処理法或いは塗布処理
法によつて金属Cr換算で片面当り5〜150mg/m2
のクロム付着量の無機物系第1層のクロメート処
理層を設け、該クロメート被膜の上層に樹脂含有
量が50〜400g/とクロム成分がその樹脂含有
量の1/50〜1/1の比率で混合してかつ、常温
の粘度が3〜50センチポアーズ、電気伝導度が2
〜30ms/cmのクロム成分含有樹脂水溶液を−80
〜−100KVの電圧を印加して毎分2万〜4万5
千回で回転する回転体に衝突させてマイナスに荷
電した霧化粒子とする静電霧化法によつて、片面
当りクロム付着量を3〜180mg/m2塗布する樹脂
含有クロメート処理層を設け、加熱温度50〜350
℃で加熱処理する二層型クロメート被膜金属表面
処理鋼板の製造方法である。 (作用) 以下本発明について詳細に説明する。 本発明においては、先ず金属表面処理鋼板の表
面に、Cr6+を主成分とする水溶液を用いて、電解
処理法或いは塗布処理法によつて、第1層に所定
量のクロメート被膜層を施す。 次いで、このまま或いは乾燥した該クロメート
被膜表面に対して、前記した構成と性状のクロム
成分含有樹脂水溶液を−80〜−100KVの電圧を
印加して毎分2万〜4万5千回で回転する回転体
に衝突させてマイナスに荷電した霧化粒子の状態
で、この霧化溶液の吐出口とアースされた被処理
の金属表面処理鋼板との間で形成された静電界を
通じて、プラスに荷電された金属表面処理鋼板に
付着させる。静電霧化の際、印加する電圧が−
80KVより低いと回転体に衝突させ霧化した粒子
内での荷電量が少ないために粒子間の反撥力が弱
く、また粒子の微細化もし難いので金属表面処理
鋼板に均一に付着しない。一方、−100KVより高
い電圧では静電界を移動する霧化粒子が微細化し
過ぎて排気流の影響を受け、不均一に付着する。
このような理由から、霧化粒子の荷電圧を−80〜
−100KVとした。また、クロム含有樹脂水溶液
を回転体に衝突させて霧化する回転数が毎分2万
回以下の低速回転では、霧化粒子が大きすぎて斑
点上の不均一な付着層を形成する。その反対に4
万5千回を越える高速回転になると超微粒子とな
つて排気流の影響を受けて不均一な付着層を形成
する。従つて、静電霧化の際の回転体の回転数
を、毎分2万〜4万5千回とした。金属表面処理
鋼板クロム含有樹脂水溶液所定量を供給する事に
より、マイナスに荷電した霧化粒子は吐出口から
噴霧すれば相互に反撥し合い凝集する事なく、均
一な分布状態で、金属表面処理鋼板に向かつて飛
び出し、金属表面処理鋼板が均一に被覆される。
特にクロム含有樹脂水溶液供給量と被金属表面処
理鋼板の移動速度(通板速度)を制御すれば任意
の被膜量(被膜厚さ)に調整できる。 この方法によれば、第1層を形成するクロメー
ト浴及び第1層のクロメート被膜の溶出物質が第
2層のクロメート浴に混入して構成の変化や性状
の劣化をもたらす事もなく、第2層のクロメート
被膜の付着を容易にする。それと同時に、第2層
を形成する樹脂含有クロメート浴は、上記の方法
によつて第1層のクロメート被膜に噴霧被覆され
た後、樹脂成分の濡れ性によつて広く被覆し、さ
らにその後の加熱処理によつて、クロメート浴中
のCr含有成分と樹脂及び第1層クロメート被膜
表面のCr含有成分と樹脂との重合反応によつて
均一な被覆効果、第1層と第2層の密着性向上効
果と、これに伴なう性能向上が併せ得られる。 すなわち、本発明は、金属表面処理鋼板のクロ
メート二層被膜と処理浴の相剰効果によつて、被
膜量の如何にかかわらず、均一被覆性にすぐれ、
外観性能、耐食性能、塗装性能にもすぐれた高性
能、クロム含有樹脂被膜を形成する。 本発明においては、亜鉛又は亜鉛合金メツキ鋼
板、アルミ又はアルミ合金メツキ鋼板、或いは鉛
又は合金メツキ鋼板等の金属表面処理鋼板の表面
に、メツキ直後或いはアルカリ系浴等による活性
化処理を施した後、Cr6+を主成分とする無機系ク
ロム化合物の水溶液を用いて第1層のクロメート
被膜層を設ける。 このクロメート処理は、樹脂を含有する有機物
系クロム化合物の水溶液を用いて通常のロールコ
ーター塗布方法などが採用されるが、付着量が特
に少ないと被膜を均一に付着することが困難であ
る。また、本発明では有機樹脂を含むクロメート
被膜で、第1層と第2層を形成した場合、前記し
た如く、これらの有機物の官能基が水分を吸収し
また被膜中に水分が侵入し、裸耐食性を劣化せし
める傾向が見られる。 従つて、本発明では第1層のクロメート被膜量
の制御が容易な事及び第2層の有機物系被膜が水
分が侵入した場合でも、第1層の無機物系クロム
化合物のクロメート被膜により、金属表面に到達
する水分を防止する効果がある。この場合のクロ
メート被膜の処理浴及び処理方法は特に限定され
るものではないが、例えば以下のようなCr6+を主
成分として含有する無機系クロム化合物を含有す
る水溶液とクロメート被膜の被覆方法を用いて、
以下に例示するような方法で行なうとよい。 すなわち、 (a) CrO3−SiO2(ケイ酸ゾル)系浴、 (b) CrO3−SO4 2-系浴、 (c) CrO3−SiO2−PO4 3-系浴 (d) CrO3−SiO2−NH4F−H2ZrF6系浴 等或いはこれらにCr3+イオンが含有されたクロメ
ート浴が用いその電解処理法は、常温〜80℃の浴
温において、電流密度10〜100A/dm2、電解処
理時間0.3〜15秒間の陰極電解処理或いは該陰極
電解処理後に0.1〜1秒間の同様の条件での陽極
電解処理で行なわれる。 又、塗布処理方法は、これらのクロメート浴を
常温〜80℃の処理浴温度で、1〜15秒間の処理時
間の浸漬処理、スプレイ処理、ロールコーター処
理などを行なつて余剰のクロメート浴を、払拭ロ
ール或いは高圧ガス気体を用いて払拭して所定量
の目的とするクロメート被膜量を制御する。 而して、この第1層のクロメート被膜を形成す
るため無機系クロメート浴を用いてクロメート被
膜量を金属クロム量換算で片面当り5〜150mg/
m2の付着量に限定する。 Cr付着量が5mg/m2未満では、該クロメート
被膜で金属表面処理鋼板の表面を均一に被覆する
事が困難であり、第2層の有機樹脂を含有するク
ロメート被膜がこの第1層表面に施されても、腐
食環境に長期間曝された場合に第2層に侵入した
腐食水溶液が容易に第1層の被膜の金属表面に到
達し、耐食性或いは塗装後の耐食性等を劣化す
る。 又、Cr付着量が150mg/m2を越えると、第1層
の性能向上効果が飽和すると共に、加工によつて
クロメート被膜にクラツクを生成し、これが起点
となつて第2層に伝播し、耐食性及び塗装後耐食
性を劣化する。 従つて、第1層のCr付着量は片面当り5〜150
mg/m2、好ましくは10〜100mg/m2である。 次いで、第1層のクロメート被膜処理後そのま
ま或いは水洗後、又これらの乾燥・熱処理を行な
つた後、第2層の樹脂クロメート被覆処理を施
す。 クロム成分を含有する樹脂水溶液は第1図及び
第2図に示す様な静電霧化塗布装置を用いて、マ
イナスに荷電したクロム含有樹脂水溶液の霧化粒
子をプラスに荷電した第1層がクロメート被膜の
金属表面処理鋼板に噴霧、均一に付着せしめる。 すなわち、クロム成分を含有した樹脂溶液1を
溶液タンク2から、目的の被膜量と金属表面処理
鋼板6の通板スピードに対応して、ポンプ3によ
り所定量の溶液を静電霧化する霧化装置4に供給
される、この霧化装置4は、エアータービン5に
結合され、第2図にその拡大模式図を示すよう
に、供給溶液が高速回転(20000〜45000RPM)
Aに霧化される。この静電霧化装置4に供給され
た溶液1は、エアータービン5で高速回転する第
2図の回転体部分Aに溶液供給パイプBから供給
された溶液1が回転体部分の表面Cにつきあた
り、回転体AとA′との間に設けられた小径(通
常直径1〜5mm)Dを通り、回転体Aの先端部分
F面を流れて最先端部分Eに到達する。 溶液1はこのF面を流れていく過程において、
高速回転に基づく遠心力によつて非常に均一に霧
化され、最先端部分Eから均一な粒径で飛び出
す。一方、この静電霧化装置4に高電圧(通常−
80KV〜−100KV)を荷電しておく事により、霧
化装置4に供給された溶液はマイナスに帯電さ
れ、霧化装置を飛び出した霧化粒子Gはマイナス
に荷電される。 而して、このマイナスに荷電された霧化粒子G
は互いに反撥し合つて凝集する事なく、もつとも
近くにあるアースすなわちプラスに荷電された金
属表面処理鋼板6に向つて、均一に飛び出し付着
される。その結果として、粒子が金属表面処理鋼
板表面に均一に付着する。 また、被処理材の被膜量は、溶液供給ポンプ3
の調整によつて、被処理鋼板6の通板スピードに
よつて任意に変える事が容易であり、通板スピー
ドを高速化する場合にはこの静電霧化装置4を多
段にならべれば容易に対応できる、勿論、板巾の
広さに対応して、板巾方向に多段に並べて、広巾
後処理材への対応も容易である。 次に、このような塗布方法において、金属表面
処理鋼板表面における均一霧化粒子の被覆は極め
て均一に積層された状態で付着しているが、極め
て微細な粒子といえども被覆処理後の加熱処理に
おいて広がり、均一被覆性にすぐれる事も重要で
ある。このためには、クロメート処理浴の構成、
性状及び熱処理温度が重要である。 而して、被膜量の如何にかかわらず、均一被覆
性、外観性能、塗装性能、塗装性能にすぐれた被
膜を得るためには、以下の様に、処理浴の構成、
性状と加熱温度を規制する。 すなわち、クロム成分を含有する樹脂処理浴の
樹脂濃度は50〜400g/、クロム成分の含有量
が樹脂含有量に対して1/50〜1/1の比率で含
有され、粘度が3〜50センチポアーズ、電気伝導
度2〜30ミリジーケンス/cm(ms/cm)からな
るクロム含有樹脂溶液を使用する。 樹脂濃度が50g/未満でクロム成分の含有量
が樹脂濃度の1/50〜1/1の比率で含有される
クロム含有樹脂水溶液は、静電霧化塗装後におい
て第1層のクロメート処理後の金属表面処理鋼板
表面上で処理溶液の濡れ拡がり性が劣り、又加熱
処理を施しても充分な均一被覆効果が得られず、
均一被覆性、処理外観、耐食性、塗装性能が劣
る。 また、樹脂濃度が400g/を越えてクロム成
分の含有量が樹脂濃度の1/50〜1/1の比率で
含有されるクロム含有樹脂水溶液は、これら溶液
の粘度が高くなり、静電霧化塗装後及び加熱処理
工程において、処理浴の金属表面処理鋼板表面上
での濡れ拡がりに時間がかかり、高速処理におい
てクロム含有樹脂被膜を均一に形成するのに不利
であり、均一外観性能、被膜の性能等を劣化す
る。 従つて、本発明においては、樹脂濃度は50〜
400g/、好ましくは15g/〜300g/であ
る。 尚、本発明に使用される樹脂は、特に規定する
ものではないが、例えばアクリル樹脂、エポキシ
樹脂、フエノキレン樹脂、フツ素樹脂、或いはフ
エノール樹脂等が単体又は2種以上混合して使用
される。これらの樹脂は、水溶液に各々50〜400
g/含有された溶液として使用する。 さらに、本発明に使用されるクロム含有樹脂水
溶液は、塗布後施される加熱処理において、クロ
メート浴中のクロム成分と樹脂或いは第1層のク
ロメート被膜と第2層の樹脂との加熱重合によつ
て被膜を高速短時間で形成することが重要であ
る。この加熱重合を促進するために、クロメート
浴中に予じめ硬化促進剤を0.5g/(例えば、
リン酸)程度を添加してもよい。 さらに、本発明において樹脂に対してクロム成
分が1/50〜1/1の比率で含有される。すなわ
ち、クロム成分はCr量として1g/〜250g/
の範囲で本発明に使用される溶液に添加すると
共に、樹脂含有量の1/50〜1/1の比率で添加
する。このクロム成分はCr6+を主成分として使用
するが、加熱処理して形成される被膜の耐食性、
塗装性能の確保に重要である。而して、加熱処理
において樹脂とクロム成分が重合して、耐食性、
塗装性能にすぐれたクロメート被膜が形成される
が、樹脂含有量の1/50未満のクロム含有量では
耐食性能を充分に確保することが困難である。す
なわち、樹脂成分を主体とする被膜が形成される
ので本発明の目的の性能が得られにくい。 一方、樹脂含有量に対してクロム含有量が1/
1を越える比率で含有されると、処理浴自体の均
一混合が充分に行なわれ難く、また静電塗装後樹
脂の濡れ拡がり効果による均一被覆性の欠如、第
1層クロメート層との加熱重合の劣化等により耐
食性の劣化、第1層と第2層のクロメート被膜の
密着性の劣化等の欠点を生じる。従つて、本発明
においては、樹脂濃度の1/50〜1/1の範囲の
比率のクロム成分が処理浴に含有される事が必要
であり、好ましくは1/30〜1/5の比率であ
る。 また、このクロム成分は、Cr6+を主成分として
含有され、加熱処理工程において樹脂と反応し
て、Cr3+を主体とする被膜が形成されるが、処理
浴中に予じめCr3+として全クロム中の40%以下の
比率の範囲でCr3+を混合してもよい。 而して、本発明に使用される処理浴に必須成分
として、樹脂と共に含有されるクロム成分は、ク
ロム酸、重クロム酸塩、クロム酸塩の各々の1種
又は2種以上が使用できる。そして、前記の樹脂
含有量に対応して、Cr量に換算して上記規定の
範囲で、クロム酸、クロム酸塩等の形態で混合さ
れる。尚、このクロム成分と樹脂成分を含有した
クロメート処理浴の作成にあたつては、使用され
る樹脂成分の安定なPH領域と対応したクロム成分
を使用するのが好ましい。例えば、酸性域で安定
なアクリル樹脂を使用する場合にはクロム成分と
してクロム酸を主成分として使用し、また中性域
で安定なエポキシ樹脂を使用する場合にはクロム
成分としてクロム酸アンモニウムを主成分と使用
する方法が採られる。すなわち、樹脂成分とクロ
ム成分が混合されたクロメート溶液の経時安定性
の点から共に安定な領域で混合使用するのが好ま
しい。 次に、このクロム成分と樹脂成分を主体とする
処理溶液の性状として、静電霧化塗布方式によ
り、本発明の目的とする効果を得るためには以下
のように規定する。先ず処理浴の粘度は、常温に
おいて3〜50センチポアーズの粘度の範囲で使用
する事が必要である。 すなわち、粘度が3センチポアーズ未満では、
塗布直後に金属表面処理鋼板上での処理浴の濡れ
拡がり速度が速く、短時間で均一に粒子と粒子の
間〓処理浴が被覆する効果を有する反面、加熱処
理による被膜の焼付け付着処理迄の間に、付着物
が流動され、均一被覆性を阻害する。一方、粘度
が50センチポアーズを越える場合には、静電塗布
された粒子の間〓処理浴の濡れ拡がり効果によつ
て均一に被覆されるためには可成りの保定時間が
必要とされる。したがつて、高速処理において、
均一被覆性にすぐれた良好な外観性能を得るため
には不利である。 本発明においては、処理浴の粘度が常温で3〜
50センチポアーズ、好ましくは4〜30センチポア
ーズである。さらに、本発明においては、処理浴
をマイナスに帯電した均一な粒径の霧化粒子とし
て塗布する事が必要であり、静電霧化装置におい
てこの霧化粒子を生成させるのに処理浴の伝導性
が重要な要因となる。すなわち、本発明に使用れ
される処理浴の電気伝導度は、常温で2〜30ミリ
ジーケンス/cm(ms/cm)に規制される。処理
浴の電気伝導度が2ms/cm未満の場合、処理浴
の抵抗値が大きいので処理浴を帯電させるために
非常に大きな高電圧が要求され、操作時の安全性
の点で問題があると同時に均一な粒径のマイナス
に荷電した霧化粒子を作成するのが困難である。 一方、処理浴の電気伝導度が30ms/cmを越え
る場合には、本発明に使用される範囲の電圧下に
おいて溶液に流れる電流が大きくなり、作業の安
全性で極めて困難となる。従つて、本発明に使用
される処理浴の電気伝導度は、常温で2〜30m
s/cmで使用される。 上記の様に、クロム成分を含有する樹脂系処理
浴の組成、性状のものを使用する事によつて、第
1層のクロメート処理を施された金属表面処理鋼
板状に均一な塗布が可能であるが、外観性能及び
被膜性能にすぐれた被膜を形成するためには、加
熱温度50〜300℃、の範囲で加熱処理を行なつて、
被処理材と塗布、付着物を結合せしめると同時
に、付着物自体も安定な被膜として形成させる事
が必要である。この場合、その加熱温度が50℃未
満では、付着物と被処理材との強固な結合効果が
得られず、また付着物自体もクロムと樹脂分との
硬化重合反応も充分でなく、性能のすぐれた被膜
が形成され難い。 一方、加熱温度が350℃を越える場合、本発明
の処理浴に使用される樹脂分が分解される危険性
があり、形成された被膜の耐食性、塗装性能が劣
化する。従つて、加熱温度は50〜350℃、好まし
くは100℃〜250℃である。 さらに、このようにして形成された被膜は、均
一被覆性にすぐれ、外観も良好であるが、耐食性
能の点から被膜中のクロム量が確保されている事
が必要である。すなわち、金属クロム量換算で片
面当りのCr付着量が3〜180mg/m2に規制され
る。Cr付着量が3mg/m2未満の場合には、被膜
中のCrの作用による耐食性能或いは塗装後耐食
性能等の性能特性の確保が困難であり、またCr
付着量が180mg/m2を越える場合は耐食性能の向
上効果が飽和すると共に、加工時に被膜の部分的
な剥落現象所謂カジリ現象が発生し易すくなるた
めかむしろ加工後の耐食性能が劣化する。従つ
て、本発明においては、Cr付着量として3〜180
mg/m2、好ましくは、10〜120mg/m2である。 尚、本発明において使用される処理浴は、クロ
ム成分及び樹脂成分を主要成分として構成される
が、前記の処理浴の性状を損なわない範囲におい
て、被処理材との反応性を向上するのに効果があ
るSO4 2-、PO4 3-等のアニオン或いは被膜の塗料
密着性を向上するのに効果があるCo2+、Ni2+
のカチオンが、各々単独或いは複合して添加され
てもよい。 或いは、本発明の被膜性能のより一層の性能向
上等を目的として、本発明に使用されるクロメー
ト浴の構成、性状を損なわない範囲で、シリカゾ
ル、アルミナゾル、ケイ酸塩等の酸化物或いはク
ロメート被膜の着色を目的としてカーボンブラツ
クの微細粉末等の着色顔料、さらにはクロメート
被膜の溶接性向上を目的としたリン鉄粉末の導電
顔料等を添加したクロメート処理浴を使用しても
よい。 一方、本発明の方法で形成せしめられたクロメ
ート被膜の外観を白色透明化するために、クロメ
ート被膜中に存在するCr6+を還元せしめる方法を
本発明のクロメート被膜に施してもよい。すなわ
ち、例えば加熱処理せられたクロメート被膜を電
導性塩(塩化アンモニウム、炭酸アンモニウム
等)を含有する水溶液中で陰極電解処理を付与す
る方法、或いは抱水ヒドラジン、ハイドロキノン
等の還元剤を含有する水溶液中への浸漬、スプレ
イ処理等の方法によつて、各々被膜中のCr6+
Cr3+への還元、溶解除去等が行なわれ、被膜の白
色透明化、被膜の更に一層の不溶解化等が促進さ
れる。これらの方法が本発明の方法のクロメート
被膜に施されても、何ら性能特性に悪影響を与え
るものではなく、むしろ場合によつては性能向上
をもたらすものであり、本発明を損なうものでは
ない。 以上の如く、本発明の方法によれば、第1層の
無機系のクロメート被膜層と第2層の有機樹脂を
含有するクロメート被膜層との複層効果および第
2層の樹脂含有クロメート被膜形成のための適正
な処理浴の構成、性状、被膜形成方法との複合効
果によつて、次のようなすぐれた作用効果が得ら
れる。 (1) 複層被膜の形成による重畳効果により、単層
のみのクロメート被膜形成と比較して、クロメ
ート被膜のピンホールの生成が少なくなり均一
被覆性にすぐれ、外観性能及び耐食性が向上す
る、 (2) 第2層の樹脂含有クロメート被膜の形成によ
り、樹脂含有成分の効果によつて、本製品が加
工される場合の湿潤効果によつてクロメート被
膜の損傷が防止され、加工性及び加工後の耐食
性向上効果が得られる。 (3) 上記(2)と同一理由により、塗装を施して使用
される場合、塗料密着性向上効果は著しい。 (4) 第2層の有機樹脂含有クロメート被膜は、腐
食環境に長期間経時された場合、有機樹脂はそ
の官能基が水分を吸収し易すく、したがつて樹
脂含有クロメート被膜層中への水分が侵入され
るが、本発明の2層型被膜の構成では第1層の
無機物系クロメート被膜の存在によつて水分或
いは腐食水溶液が金属表面処理鋼板の表面に到
達するのが防止される、その結果として、裸使
用時の耐食性にすぐれ、また塗装材に対して
も、塗装欠陥部或いは塗膜を通つて侵入した食
水溶液に対して同様の効果が得られ、経時後の
塗料密着性及び塗装後の耐食性向上効果が極め
てすぐれている。 (5) 第2層の被膜形成方法として、クロメート浴
が静電霧化法による付着方式を用いるため、第
1層形成のためのクロメート浴と第2層の処理
浴が非接触の状態で、プラスに荷電された第2
層のクロメート浴の霧化粒子がマイナスに荷電
された第1層のクロメート被膜を施された被処
理材に付着、被覆される。 その結果として、第1層のクロメート処理浴
と第2層のクロメート処理浴が混合して、経時
によりゲル化する現象、或いは第2層のクロメ
ート被膜の性能劣化等が生じない利点が得られ
る。また同時に、プラスに荷電された粒子のマ
イナスに荷電された被処理材への付着による塗
布方式のため、第2層の被膜形成のクロメート
浴を効率よく、さらに霧化処理浴の供給を定量
的に行なう事によつてクロメート被膜量(厚
さ)の調整を任意に行なうことが可能である。 従つて、被膜厚さの薄い被膜から厚い被膜ま
で任意に制御可能であり、均一被覆性にすぐれ
た被膜を得るのが、他の処理方式に比して、有
機樹脂を含有するクロメート処理浴を用いるに
もかかわらずにすぐれている。 (6) 第2層のクロメート被膜を付着後の加熱処理
工程において、第2層被膜中のクロム成分と樹
脂成分、第1層のクロメート被膜中のクロム成
分と第2層の樹脂成分との各々加熱重合反応に
よつて、第2層の被膜形成と同時に第1層の被
膜と密着性のすぐれた複層被膜の形成が可能と
なる。 等の作用効果が得られる。 (実施例) 本発明の作用効果を明確にするため、幾つかの
実施例及び比較例を挙げ具体的に説明する。 実施例 1 メツキ量が片面当りの付着量で各々20g/m2
電気亜鉛メツキ鋼板を被処理材として用い、板巾
900mm、通板スピード90m/minの条件で、本発
明の二層処理を施した、すなわち、第1層につい
ては第1表に示すクロメート浴及び処理方法でク
ロメート被膜層を設け、次いで第1図に示した静
電塗布装置を用い、第1表に示した構成、性状の
処理浴を用いて、加熱処理を行なつて本発明の処
理を施した。 尚、併せ同一の被処理材を用いて、第1表に示
す各種方法のクロメート処理を行なつた場合の比
較例の処理条件、クロメート被膜性状を示す。 尚、本発明の実施に際しては、 (1) 第2層のクロメート被膜形成のための処理浴
の基本構成平均分子量約150000のエマルジヨン
タイプのアクリル樹脂を用いるとともに、クロ
ム成分としてCrO3及びCr6+の一部をアルコー
ルで還元したCr3+を、また硬化剤としてさく酸
アルミを添加したクロム成分含有樹脂溶液を使
用 (2) 静電塗布方法;第1図に示した静電塗布装置
を用い、通板スピード、板巾に対応させ、定量
ポンプで目的とする付着量に相当するクロメー
ト処理浴を供給するとともに、エアタービンを
2.0Kg/cm2で25000回転させ、被処理材をプラス
極、エアタービンをマイナス極として、この間
に100KVの電圧を印加して噴霧粒をマイナス
に帯電させ、静電霧化粒子を定速で通板されて
いる電気亜鉛メツキ鋼板に供給、付着せしめ
た。 (3) 加熱処理;板温180℃で10秒間の加熱処理を
熱風炉で実施した。 以上の方法で処理浴の影響、クロメート被膜量
の影響を中心としたその被膜性能も併せ検討し
た。第1表に本発明の方法による処理条件を、ま
た第2表に本発明の方法によるクロメート被膜の
性能特性の評価結果を示す。 尚、評価方法及び評価基準は、以下の方法で実
施するとともに性能についてはほぼ同一クロム付
着量のクロメート被膜を形成されたもの同志につ
いて、相対的に比較検討を行なつた。 Γ評価方法及び評価基準 処理状況と処理外観 処理時及びクロメート被膜形成後に、各々肉
観観察を行ない、以下の評価基準で評価を行な
つた。 ◎…処理時にクロメート浴が均一に両面に付着さ
れるとともに、加熱処理後の形成されたクロ
メート被膜が色むら、斑点模様等、生成され
ずに均一に形成 ○…処理時クロメート浴が部分的に付着むらを生
じて付着されるが、加熱処理後は比較的均一
なクロメート被膜形成 △…処理時に処理浴が発泡或いは濡れ不良等の処
理付着むらが可成り生成され、かつ加熱処理
後においてもクロメート被膜の付着量(厚
さ)むらが明確に認められるもののクロメー
ト被膜が全面に形成 ×…処理時において処理浴の液切れ或いは濡れ不
良等の現象によりクロメート浴の付着してい
ない部分が認められ、また加熱処理によるク
メート被膜形成後も被膜形成が認められない
部分が認められる場合 クロメート被膜の均一被覆性 評価材に対して、2×2mmの評価面につい
て、ビーム径2μのCr特性X線を1000×1000個
のマス目に照射し、各マス目に対してCrのX
線カウント数(CPS)を測定した。 一方、標準試料について、化学分析値とそれ
に相当するX線カウント数(CPS)を測定し、
上記の測定カウント数と対比して、評価材の各
マス目のCr付着量を求める事によつてミクロ
的なクロメート被覆性を評価した。 尚、評価基準は以下の方法に拠つた、すなわ
ち、第1表に示す平均化学分析値(mg/m2
に対して、 ◎…(±10%以内)のCr付着量が評価面・
全面のCr付着量に対して、85%以上の面積
率を占める場合、 ○…(±10%以内)のCr付着量が評価面・
全面のCr付着量に対して、85%未満〜65%
以上の面積率を占める場合、 △…(±10%以内)のCr付着量が評価面・
全面のCr付着量が65%以上の面積率を占め
るが、(±30%以上)のCr付着量が20%以
上の面積率で存在する場合 ×…Cr付着量の検出されない部分が評価面に
2.5%以上の面積率で存在する場合、 耐食性 塩水噴霧試験(JIS−Z−2371)により、(a)
平板のまま及び(b)0.8mmの板厚に対して、ブラ
ンクサイズ200×200mmに切り出し、これを高さ
30mmの角筒加工を行なつたものについて、各々
所定時間評価テストを実施して、以下の評価基
準で評価を行なつた。 (a) 平板の耐食性 ◎…白錆発生率1%未満 ○…白錆発生率1%以上〜5%未満 △…白錆発生率5%以上〜20%未満 ×…白錆発生率20%以上 (b) 加工後の耐食性 ◎…白錆発生率5%未満 ○…白錆発生率5%以上〜15%未満 △…白錆発生率15%以上〜30%未満 ×…白錆発生率30%以上 塗料密着性 メラミン−アルキツド系樹脂を25μ厚さ塗装
焼付け後、0.8mm板厚の評価材を用いて、7mm
高さのエリクセン加工を行なつた。 −1 評価法(A) エリクセン加工後、その表面にセロテープ
を付着後剥離して塗膜の剥離状況を以下の評
価基準で評価 ◎…塗膜剥離殆んど認められない ○…1mm径程度以下の塗膜剥離が5点以下 △…1mm径程度以下の塗膜剥離が5点より多
く発生或いは評価面の10%以下の可成り大き
な面積の塗膜剥離発生 ×…明りように認められる大きな面積の塗膜
剥離が10%より多く発生 −2 評価法(B) 塗装材を30分間沸騰水に浸漬後、乾燥して
24時間放置後にエリクセン加工を行ない、上
記と同様の剥離試験を実施し、上記と同基準
で評価 塗装後耐食性 100×150mmサイズの評価材に対して、メラミ
ン−アルキツド系塗料を25μ厚さ、塗装・焼付
後、メツキ層の表面に達するスクラツチ疵を入
れ、塩水噴霧試験を所定時間行なつて、以下の
評価基準によりその塗装後耐食性能を評価し
た。 ◎…スクラツチ部からのフクレ巾が最大3mm未
満で、その他平面部からのブリスターの発生
3点以下。 ○…スクラツチ部からのフクレ巾が最大6mm未
満或いは、その他平面部からのブリスターの
発生7点以下 △…スクラツチ部からのフクレ巾が最大10mm未
満或いは、その他平面からのブリスターの発
生10点以下 ×…スクラツチ部からのフクレ巾が最大10mm以
上の場合或いはその他平面部からのブリスタ
ーの発生11点以上。
(Field of Industrial Application) The present invention relates to a method for producing a metal surface-treated steel sheet with excellent corrosion resistance and coating performance, in which a two-layer chromate coating is applied to a metal surface-treated steel sheet. The metal surface-treated steel sheets mentioned here include zinc and zinc alloy plated steel sheets, lead and lead alloy plated steel sheets,
It is a steel plate plated with metal, such as aluminum and aluminum alloy plated steel plate. Specifically, galvanized steel sheets and zinc alloy-plated steel sheets include: (a) galvanized steel sheets that contain elements that are unavoidably mixed in as impurities by electroplating or vacuum evaporation plating; and (b) galvanized steel sheets with an Al content of 0.1 to 0.3. %, other substances include Pb, Cd, Fe,
Hot-dip galvanized steel sheet containing one or more elements such as Sb and unavoidable impurity elements (c) Fe-Zn alloy-plated steel sheet containing 5 to 90% Fe and unavoidable impurity elements (d ) Zn-Ni alloy plated steel sheet containing 5 to 20% Ni and unavoidable impurity elements (e) Zn containing 3 to 60% Al or containing Si, Mg, Mitsushi metal, or unavoidable impurities
-Al alloy plated steel sheets, etc.; lead plated and lead alloy plated steel sheets include (a) lead plated steel sheets containing unavoidable impurities during the manufacturing process; (b) containing 30% or less of Sn; and in some cases Sb,
Examples include Pb-Sn alloy plated steel sheets that contain Zn or other unavoidable impurity elements; furthermore, aluminum and aluminum alloy plated steel sheets include (a) unavoidable amounts of Fe and other elements during plating; , aluminized steel sheet (b) Contains one or more of Si and Mg, and Si is 12
% or less, or an aluminum alloy plated steel plate with Mg content of 5% or less. (Prior art) Recently, users have asked us about the appearance, uniform coverage, corrosion resistance, and painting performance (paint adhesion, corrosion resistance after painting, etc.) of metal surface-treated steel sheets such as galvanized steel sheets and zinc alloy-plated steel sheets. Since there is a strong desire for an excellent treatment method, various chromate treatments are being carried out. For example, (1) a method of forming a film on the surface of a surface-treated steel sheet by applying an aqueous solution containing a chromium compound in an organic resin and then drying it (for example, JP-A-59-200768). (2) On the surface of the surface-treated steel sheet, a first layer coating is formed by applying an aqueous solution containing a chromium compound in an organic resin and then drying, and then coating the first layer coating on the surface of the first layer coating. A method of forming a second layer film by further applying a water-soluble organic resin (for example, Japanese Patent Application Laid-Open No. 14552/1983). (3) A first layer film is formed by applying an aqueous solution consisting of a chromium compound and an inorganic acid on the surface of the surface-treated steel sheet and then drying it, and then further applying an aqueous solution on the surface of the first layer film. A method of forming a second layer film by applying a synthetic organic resin (for example, JP-A-59-166678, JP-A-59-162278, JP-A-59-162279). (4) Surface-treated galvanized or alloyed galvanized steel sheet is coated with a chromium compound aqueous solution containing phosphoric acid, zinc ions, and fluorine ions to form a first layer of chromate film, and silicon dioxide is applied on top of the first layer of chromate film. A method of forming a second layer of chromate film by applying an aqueous solution of a chromium compound to which each of the above-mentioned contained ions is added (for example, Japanese Patent Application Laid-Open No. 1983-1999)
4880). etc. (Problems to be Solved by the Invention) Although the surface-treated steel sheet manufactured by the method (1) above has excellent paint film adhesion and corrosion resistance after painting, it has a problem that it is inferior in bare corrosion resistance without painting. have. In other words, since the coating formed by method (1) above contains many organic substances, when exposed to a corrosive environment for a long time without coating, the functional groups of the organic substances absorb moisture, and further tends to penetrate into the coating and deteriorate bare corrosion resistance. The surface-treated steel sheets produced by the methods (2) and (3) above are unpainted and have excellent bare corrosion resistance and paint film adhesion. However, if the drying or insolubilization reaction of the first layer chromate film is insufficient when applying the water-soluble organic resin of the second layer film onto the surface of the first layer film, this film may The components are eluted into the water-soluble organic resin of the second layer, gelling the water-soluble organic resin, resulting in deterioration of the bath life of the water-soluble organic resin bath and deterioration of the coating performance of the second layer. Therefore, in order to sufficiently dry or insolubilize the first layer coating, a drying device such as an induction heater or an infrared heater is required. There were also issues that required time. Furthermore, over time, the organic resin in the second layer organic coating reacts with the Cr 6+ in the first layer coating, resulting in deterioration of coating performance. In addition, when applying these organic resins or aqueous solutions of organic resins containing chromium compounds to the surface of surface-treated steel sheets, a coating method using a roll coater is mainly used to ensure good appearance performance and uniform coverage of the film. are doing. This method is advantageous for uniform coating when a thick coating layer with a thickness of 1μ or more, preferably 3μ or more is applied, but it is advantageous for uniform coating when a thin coating layer of less than 1μ is applied, improving appearance performance and spreading properties. Therefore, it is difficult to form a coating with excellent corrosion resistance. Further, in the method (4) above, the chromate film of the first layer is eluted into the second layer forming treatment bath due to long-term operation. Therefore, in order to form a chromate film with good performance in the second layer, it is necessary to control the ions eluted from the first layer film, and it is necessary to perform complicated bath composition adjustment and management of the second layer treatment bath. There were some problems. Furthermore, Japanese Patent Application Laid-Open No. 52-10834 discloses a chromate treatment method in which an aqueous solution containing a chromium compound, colloidal silica, etc. is applied to a metal surface using an electrostatic atomizer. However, in this method, an aqueous solution containing a chromium compound is applied in an atomized state under electrostatic charge, so the atomized particles are efficiently attached to the metal surface, but the distance between the attached particles is small. There was a problem that the uniform coverage of the chromate film deteriorated and the corrosion resistance deteriorated. The present invention solves the performance problems and processing problems of the various chromate treatment methods described above, and provides an industrially stable chromate treatment method with excellent appearance, uniform coverage, corrosion resistance, and coating performance. It is intended to be formed on the surface of a steel plate. (Means for solving the problem) Excellent appearance, coating uniformity, corrosion resistance, and painting performance of metal surface-treated steel sheets such as zinc or zinc alloy plated steel sheets, aluminum or aluminum alloy plated steel sheets, and lead or lead alloy plated steel sheets. As a result of various studies on manufacturing methods for metal surface-treated steel sheets with a two-layer chromate coating, we found that the composition and properties of the second layer chromate bath were adapted to the uniform formation of electrostatically atomized particles, and that this chromate bath was used in the first layer. A second layer of chromate film is deposited and formed on a metal surface-treated steel sheet with a chromate film by electrostatic atomization, and a second layer of film is formed by mixing a chromate bath that forms a chromate film on the first layer. The chromate bath for formation is not contaminated, and the second layer of chromate film can be provided at a predetermined amount regardless of the amount (thickness) of the second layer, and the superimposed effect with the first layer of chromate film can be avoided. It was thus discovered that a film with excellent uniformity could be obtained. The present invention was constructed based on this knowledge,
The gist of this is that by applying an electrolytic treatment method or a coating treatment method using an aqueous solution containing Cr 6+ as the main component to a steel sheet that has been subjected to metal surface treatment, 5 to 150 mg/m 2 of metal Cr can be added per side to the steel plate in terms of metal Cr.
An inorganic first chromate treatment layer with a chromium adhesion amount of When mixed, the viscosity at room temperature is 3 to 50 centipoise, and the electrical conductivity is 2.
~30ms/cm of chromium component-containing resin aqueous solution at -80
20,000 to 45,000 per minute by applying a voltage of ~-100KV
A resin-containing chromate treatment layer is applied using an electrostatic atomization method in which negatively charged atomized particles are produced by colliding with a rotary body that rotates 1,000 times to form a chromium coating of 3 to 180 mg/ m2 per side. , heating temperature 50-350
This is a method for producing a two-layer chromate-coated metal surface-treated steel sheet that is heat-treated at ℃. (Function) The present invention will be explained in detail below. In the present invention, first, a predetermined amount of chromate coating layer is applied to the surface of a metal surface-treated steel sheet as a first layer by electrolytic treatment or coating treatment using an aqueous solution containing Cr 6+ as the main component. . Next, a chromium component-containing resin aqueous solution having the above-described composition and properties is applied to the surface of the chromate film, either as it is or dried, at a voltage of -80 to -100 KV and rotated at a speed of 20,000 to 45,000 times per minute. The atomized particles are negatively charged by colliding with a rotating body, and then become positively charged through the electrostatic field formed between the discharge port of this atomized solution and the grounded metal surface-treated steel plate to be treated. It is attached to a metal surface-treated steel plate. During electrostatic atomization, the applied voltage is -
If the voltage is lower than 80 KV, the amount of charge in the particles that are atomized by colliding with the rotating body is small, so the repulsive force between the particles is weak, and it is also difficult to make the particles finer, so they do not adhere uniformly to the metal surface-treated steel sheet. On the other hand, at a voltage higher than -100KV, the atomized particles moving in the electrostatic field become too fine and are affected by the exhaust flow, causing them to adhere unevenly.
For this reason, the charging voltage of the atomized particles is set to −80~
-100KV. In addition, when the chromium-containing resin aqueous solution is collided with a rotating body and atomized at a low rotation speed of 20,000 times per minute or less, the atomized particles are too large and form an uneven adhesion layer on the spots. On the contrary, 4
When it rotates at high speeds exceeding 5,000 times, it becomes ultrafine particles and forms an uneven adhesion layer due to the influence of the exhaust flow. Therefore, the number of rotations of the rotating body during electrostatic atomization was set to 20,000 to 45,000 times per minute. Metal surface treated steel sheet By supplying a predetermined amount of chromium-containing resin aqueous solution, the negatively charged atomized particles repel each other and do not aggregate when sprayed from the discharge port, and are evenly distributed to form a metal surface treated steel sheet. The metal surface treated steel sheet is uniformly coated.
In particular, by controlling the supply amount of the chromium-containing resin aqueous solution and the moving speed (passing speed) of the steel sheet to be surface-treated, the coating amount (coating thickness) can be adjusted to an arbitrary value. According to this method, the eluted substances of the chromate bath forming the first layer and the chromate coating of the first layer do not mix into the chromate bath of the second layer, causing a change in the composition or deterioration of the properties. Facilitates the adhesion of the chromate coating of the layer. At the same time, the resin-containing chromate bath forming the second layer is spray coated on the chromate coating of the first layer by the method described above, and is then widely coated due to the wettability of the resin component, followed by subsequent heating. Through the treatment, a polymerization reaction between the Cr-containing component in the chromate bath and the resin, and the Cr-containing component on the surface of the first layer chromate coating and the resin results in a uniform coating effect and improved adhesion between the first and second layers. effect and the accompanying performance improvement can be obtained at the same time. That is, the present invention has excellent uniform coverage regardless of the amount of coating due to the mutual effect of the two-layer chromate coating on the metal surface-treated steel sheet and the treatment bath.
Forms a high-performance, chromium-containing resin coating with excellent appearance, corrosion resistance, and coating performance. In the present invention, the surface of a metal surface-treated steel sheet such as a zinc or zinc alloy plated steel plate, an aluminum or aluminum alloy plated steel plate, or a lead or alloy plated steel plate is applied immediately after plating or after activation treatment with an alkaline bath or the like. , a first chromate coating layer is provided using an aqueous solution of an inorganic chromium compound containing Cr 6+ as a main component. For this chromate treatment, a conventional roll coater coating method using an aqueous solution of an organic chromium compound containing a resin is employed, but if the amount of coating is particularly small, it is difficult to uniformly adhere the film. In addition, in the present invention, when the first and second layers are formed with a chromate film containing an organic resin, as described above, the functional groups of these organic substances absorb moisture, and moisture enters the film, resulting in the formation of bare metal. There is a tendency for corrosion resistance to deteriorate. Therefore, in the present invention, it is easy to control the amount of chromate coating in the first layer, and even if moisture enters the organic coating in the second layer, the chromate coating made of the inorganic chromium compound in the first layer protects the metal surface. It has the effect of preventing moisture from reaching the. In this case, the treatment bath and treatment method for the chromate film are not particularly limited ; make use of,
It is preferable to use the method exemplified below. That is, (a) CrO 3 −SiO 2 (silicate sol) bath, (b) CrO 3 −SO 4 2- bath, (c) CrO 3 −SiO 2 −PO 4 3 -bath (d) CrO 3 -SiO 2 -NH 4 F-H 2 ZrF 6- based bath or the like or a chromate bath containing Cr 3+ ions is used for electrolytic treatment at a bath temperature of room temperature to 80°C and a current density of 10 to 80°C. A cathodic electrolytic treatment is carried out at 100 A/dm 2 for an electrolytic treatment time of 0.3 to 15 seconds, or an anodic electrolytic treatment is carried out under similar conditions for a period of 0.1 to 1 second after the cathodic electrolytic treatment. In addition, the coating treatment method is to perform immersion treatment, spray treatment, roll coater treatment, etc. at a treatment bath temperature of room temperature to 80°C for a treatment time of 1 to 15 seconds to remove excess chromate bath. The desired amount of chromate coating is controlled by wiping with a wiping roll or high-pressure gas. In order to form this first layer of chromate film, an inorganic chromate bath is used to reduce the amount of chromate film to 5 to 150 mg per side in terms of the amount of metallic chromium.
Limited to a coating weight of m 2 . If the amount of Cr deposited is less than 5 mg/ m2 , it is difficult to uniformly cover the surface of the metal surface-treated steel sheet with the chromate film, and the chromate film containing the organic resin of the second layer is coated on the surface of the first layer. Even if it is applied, when exposed to a corrosive environment for a long period of time, the corrosive aqueous solution that has entered the second layer easily reaches the metal surface of the first layer coating, degrading the corrosion resistance or the corrosion resistance after painting. Furthermore, when the amount of Cr attached exceeds 150 mg/m 2 , the performance improvement effect of the first layer is saturated, and cracks are generated in the chromate film due to processing, which become starting points and propagate to the second layer. Deteriorates corrosion resistance and corrosion resistance after painting. Therefore, the amount of Cr deposited in the first layer is 5 to 150 per side.
mg/m 2 , preferably 10-100 mg/m 2 . Next, after the first layer chromate coating treatment, the second layer resin chromate coating treatment is applied as it is or after washing with water, or after drying and heat treatment. The aqueous resin solution containing the chromium component is coated using an electrostatic atomization coating device as shown in Figs. Spray on metal surface treated steel plate with chromate coating to ensure uniform adhesion. That is, a predetermined amount of the solution is electrostatically atomized by the pump 3 from a solution tank 2 to a resin solution 1 containing a chromium component, in accordance with the desired coating amount and the speed of passing the metal surface-treated steel sheet 6. This atomizing device 4 is connected to an air turbine 5, and as shown in an enlarged schematic diagram in FIG.
A is atomized. The solution 1 supplied to the electrostatic atomizer 4 is supplied from the solution supply pipe B to the rotating body part A in FIG. , passes through a small diameter (usually 1 to 5 mm in diameter) D provided between the rotating bodies A and A', flows through the surface F of the tip end of the rotating body A, and reaches the tip end E. In the process of solution 1 flowing on this F plane,
It is atomized very uniformly by the centrifugal force based on high-speed rotation, and is ejected from the leading edge portion E with a uniform particle size. On the other hand, this electrostatic atomizer 4 is applied with a high voltage (usually -
80KV to -100KV), the solution supplied to the atomizer 4 is negatively charged, and the atomized particles G that have flowed out of the atomizer are negatively charged. Therefore, these negatively charged atomized particles G
The particles do not repel each other and aggregate, but rather uniformly fly out and adhere to the nearby ground, that is, the positively charged metallic surface-treated steel plate 6. As a result, the particles adhere uniformly to the surface of the metal-surface-treated steel sheet. In addition, the amount of coating on the material to be treated is determined by the solution supply pump 3.
It is easy to arbitrarily change the threading speed of the steel sheet 6 to be processed by adjusting the speed of the steel sheet 6. In order to increase the threading speed, it is easy to arrange the electrostatic atomizers 4 in multiple stages. Of course, depending on the width of the board, they can be arranged in multiple stages in the board width direction, making it easy to deal with wide-width post-processed materials. Next, in this coating method, the coating of uniform atomized particles on the surface of the metal surface-treated steel sheet is adhered in an extremely uniform layered state, but even if the particles are extremely fine, the heat treatment after the coating treatment is necessary. It is also important that the coating spreads well and has excellent uniform coverage. For this purpose, the composition of the chromate treatment bath,
Properties and heat treatment temperature are important. Therefore, in order to obtain a film with excellent uniform coverage, appearance performance, painting performance, and coating performance, regardless of the film amount, the composition of the treatment bath,
Regulate properties and heating temperature. That is, the resin concentration of the resin treatment bath containing the chromium component is 50 to 400 g/2, the chromium component content is contained at a ratio of 1/50 to 1/1 to the resin content, and the viscosity is 3 to 50 centipoise. , a chromium-containing resin solution having an electrical conductivity of 2 to 30 milliSequences/cm (ms/cm) is used. A chromium-containing resin aqueous solution with a resin concentration of less than 50g/1 and a chromium component content of 1/50 to 1/1 of the resin concentration should be used after the first layer of chromate treatment after electrostatic atomization painting. The wetting and spreading properties of the treatment solution on the surface of the metal surface-treated steel sheet are poor, and even if heat treatment is applied, a sufficient uniform coating effect cannot be obtained.
Uniform coverage, treated appearance, corrosion resistance, and coating performance are poor. In addition, chromium-containing resin aqueous solutions in which the resin concentration exceeds 400g and the chromium component content is 1/50 to 1/1 of the resin concentration will have a high viscosity, resulting in electrostatic atomization. After painting and in the heat treatment process, it takes time for the treatment bath to wet and spread on the surface of the metal surface-treated steel sheet, which is disadvantageous in forming a chromium-containing resin film uniformly in high-speed processing, and reduces the uniform appearance performance and the film's performance. Deterioration of performance etc. Therefore, in the present invention, the resin concentration is 50~
400g/, preferably 15g/-300g/. Although the resin used in the present invention is not particularly limited, for example, acrylic resin, epoxy resin, phenokylene resin, fluorine resin, or phenol resin may be used alone or in combination of two or more. These resins each have a concentration of 50 to 400 in aqueous solution.
g/Used as a contained solution. Furthermore, the chromium-containing resin aqueous solution used in the present invention undergoes heat polymerization of the chromium component in the chromate bath and the resin, or the chromate coating of the first layer and the resin of the second layer, during the heat treatment performed after coating. Therefore, it is important to form a film at high speed and in a short time. In order to accelerate this thermal polymerization, 0.5 g/hardening accelerator (for example,
Phosphoric acid) may be added. Furthermore, in the present invention, the chromium component is contained in a ratio of 1/50 to 1/1 to the resin. In other words, the chromium component has a Cr content of 1g/~250g/
It is added to the solution used in the present invention in a range of 1/50 to 1/1 of the resin content. This chromium component uses Cr6 + as its main component, but the corrosion resistance of the coating formed by heat treatment,
This is important for ensuring coating performance. During heat treatment, the resin and chromium components polymerize, resulting in corrosion resistance and
A chromate film with excellent coating performance is formed, but if the chromium content is less than 1/50 of the resin content, it is difficult to ensure sufficient corrosion resistance. In other words, since a film mainly composed of a resin component is formed, it is difficult to obtain the desired performance of the present invention. On the other hand, the chromium content is 1/1/1 of the resin content.
If it is contained in a ratio exceeding 1, it will be difficult to achieve sufficient uniform mixing in the treatment bath itself, and there will also be a lack of uniform coverage due to the wetting and spreading effect of the resin after electrostatic coating, and heat polymerization with the first chromate layer. Deterioration causes drawbacks such as deterioration of corrosion resistance and deterioration of adhesion between the first and second chromate coatings. Therefore, in the present invention, it is necessary that the treatment bath contain the chromium component in a ratio of 1/50 to 1/1 of the resin concentration, preferably 1/30 to 1/5. be. In addition, this chromium component contains Cr 6+ as a main component, and reacts with the resin in the heat treatment process to form a film mainly composed of Cr 3+ . Cr 3+ may be mixed as + in a proportion of 40% or less of the total chromium. As the chromium component contained together with the resin as an essential component in the treatment bath used in the present invention, one or more of chromic acid, dichromate, and chromate can be used. Then, corresponding to the resin content, chromic acid, chromate, etc. are mixed in the form of chromic acid, chromate, etc. within the range specified above in terms of Cr amount. In preparing a chromate treatment bath containing a chromium component and a resin component, it is preferable to use a chromium component that corresponds to the stable PH range of the resin component used. For example, when using an acrylic resin that is stable in an acidic region, chromic acid is used as the main chromium component, and when using an epoxy resin that is stable in a neutral region, ammonium chromate is used as the main chromium component. The ingredients and method of use are taken. That is, from the viewpoint of stability over time of a chromate solution in which a resin component and a chromium component are mixed, it is preferable to mix and use them in a range where both are stable. Next, the properties of the treatment solution mainly consisting of chromium and resin components are defined as follows in order to obtain the desired effects of the present invention using an electrostatic atomization coating method. First, the viscosity of the treatment bath must be within the range of 3 to 50 centipoise at room temperature. That is, if the viscosity is less than 3 centipoise,
Immediately after application, the treatment bath spreads quickly on the metal surface-treated steel sheet, and while the treatment bath has the effect of uniformly covering particles between particles in a short time, it also has the effect of coating the coating between particles by heat treatment. During this time, the deposits are fluidized and impede uniform coverage. On the other hand, if the viscosity exceeds 50 centipoise, a considerable holding time is required in order for the electrostatically applied particles to be uniformly coated by the wetting and spreading effect of the treatment bath. Therefore, in high-speed processing,
This is disadvantageous for obtaining good appearance performance with excellent uniform coverage. In the present invention, the viscosity of the treatment bath is 3 to 3 at room temperature.
50 centipoise, preferably 4 to 30 centipoise. Furthermore, in the present invention, it is necessary to apply the processing bath as atomized particles having a uniform particle size and which are negatively charged. Gender is an important factor. That is, the electrical conductivity of the treatment bath used in the present invention is regulated to 2 to 30 millisequences/cm (ms/cm) at room temperature. If the electrical conductivity of the treatment bath is less than 2ms/cm, the resistance value of the treatment bath is large, so a very large high voltage is required to charge the treatment bath, which may pose a safety problem during operation. At the same time, it is difficult to create negatively charged atomized particles of uniform particle size. On the other hand, if the electrical conductivity of the treatment bath exceeds 30 ms/cm, a large current will flow through the solution under the voltage range used in the present invention, making it extremely difficult to work safely. Therefore, the electrical conductivity of the treatment bath used in the present invention is 2 to 30 m at room temperature.
Used in s/cm. As mentioned above, by using a resin-based treatment bath with a composition and properties that contain chromium components, it is possible to uniformly apply the first layer of chromate treatment to the metal surface treated steel plate. However, in order to form a film with excellent appearance and film performance, heat treatment is performed at a heating temperature in the range of 50 to 300°C.
It is necessary to bond the material to be coated and the deposits, and at the same time to form the deposits themselves into a stable film. In this case, if the heating temperature is less than 50℃, a strong bonding effect between the deposit and the treated material cannot be obtained, and the hardening polymerization reaction between the deposit itself and the chromium and resin components is not sufficient, resulting in poor performance. It is difficult to form a good film. On the other hand, if the heating temperature exceeds 350°C, there is a risk that the resin component used in the treatment bath of the present invention will be decomposed, and the corrosion resistance and coating performance of the formed film will deteriorate. Therefore, the heating temperature is 50 to 350°C, preferably 100 to 250°C. Furthermore, the coating formed in this manner has excellent uniform coverage and good appearance, but from the viewpoint of corrosion resistance, it is necessary to ensure a sufficient amount of chromium in the coating. That is, the amount of Cr deposited per one side is regulated to 3 to 180 mg/m 2 in terms of the amount of metallic chromium. If the amount of Cr deposited is less than 3 mg/ m2 , it is difficult to secure performance characteristics such as corrosion resistance due to the action of Cr in the coating or corrosion resistance after painting.
If the amount of adhesion exceeds 180 mg/m 2 , the effect of improving corrosion resistance is saturated, and the corrosion resistance after processing deteriorates, perhaps because partial peeling of the coating, a so-called galling phenomenon, becomes more likely to occur during processing. . Therefore, in the present invention, the amount of Cr deposited is 3 to 180
mg/m 2 , preferably 10-120 mg/m 2 . The treatment bath used in the present invention is composed of a chromium component and a resin component as main components, but to the extent that the properties of the treatment bath are not impaired, additives may be added to improve the reactivity with the material to be treated. Anions such as SO 4 2- and PO 4 3- , which are effective, or cations, such as Co 2+ and Ni 2+ , which are effective in improving the paint adhesion of the coating, are added individually or in combination. Good too. Alternatively, for the purpose of further improving the coating performance of the present invention, oxides such as silica sol, alumina sol, silicate, etc. or chromate coatings may be used as long as the composition and properties of the chromate bath used in the present invention are not impaired. A chromate treatment bath may be used in which a coloring pigment such as fine carbon black powder is added for the purpose of coloring the chromate film, and a conductive pigment such as phosphorus iron powder is added for the purpose of improving the weldability of the chromate film. On the other hand, in order to make the chromate film formed by the method of the present invention white and transparent in appearance, the chromate film of the present invention may be subjected to a method of reducing Cr 6+ present in the chromate film. That is, for example, a method in which a heat-treated chromate film is subjected to cathodic electrolysis treatment in an aqueous solution containing a conductive salt (ammonium chloride, ammonium carbonate, etc.), or an aqueous solution containing a reducing agent such as hydrazine hydrate or hydroquinone. The Cr 6+ in each coating can be removed by immersion, spray treatment, etc.
Reduction to Cr 3+ , dissolution and removal, etc. are carried out, and the coating becomes white and transparent, and further insolubilization of the coating, etc. is promoted. Even if these methods are applied to the chromate coating of the method of the present invention, they do not have any adverse effect on the performance characteristics, but rather may improve the performance in some cases, and do not impair the present invention. As described above, according to the method of the present invention, the multilayer effect of the first inorganic chromate coating layer and the second organic resin-containing chromate coating layer and the formation of the second resin-containing chromate coating layer are achieved. The following excellent effects can be obtained by combining the appropriate treatment bath composition, properties, and film formation method. (1) Due to the superimposed effect of forming a multi-layer coating, the formation of pinholes in the chromate coating is reduced compared to the formation of a single-layer chromate coating, resulting in excellent uniform coverage and improved appearance performance and corrosion resistance. 2) Formation of the second layer of resin-containing chromate film prevents damage to the chromate film due to the effect of the resin-containing components and the moistening effect when this product is processed, improving processability and post-processing properties. The effect of improving corrosion resistance can be obtained. (3) For the same reason as in (2) above, when used after being painted, the effect of improving paint adhesion is remarkable. (4) When the organic resin-containing chromate coating layer of the second layer is exposed to a corrosive environment for a long period of time, the functional groups of the organic resin tend to absorb moisture, and therefore moisture is absorbed into the resin-containing chromate coating layer. However, in the structure of the two-layer coating of the present invention, the presence of the first layer of inorganic chromate coating prevents moisture or aqueous corrosive solution from reaching the surface of the metal surface-treated steel sheet. As a result, it has excellent corrosion resistance when used naked, and also has the same effect on painted materials as against aqueous solution that has entered through paint defects or the paint film, and improves paint adhesion and paint quality after aging. The subsequent corrosion resistance improvement effect is extremely excellent. (5) As the method for forming the second layer film, the chromate bath uses an electrostatic atomization deposition method, so the chromate bath for forming the first layer and the treatment bath for the second layer are not in contact with each other. The second positively charged
The atomized particles of the chromate bath of the layer adhere to and coat the material to be treated, which is coated with the negatively charged chromate coating of the first layer. As a result, there is an advantage that the chromate treatment bath of the first layer and the chromate treatment bath of the second layer do not mix, causing gelation over time or performance deterioration of the chromate coating of the second layer. At the same time, since the coating method relies on the adhesion of positively charged particles to the negatively charged material to be treated, the chromate bath for forming the second layer can be efficiently supplied, and the atomization treatment bath can be supplied quantitatively. By doing so, it is possible to arbitrarily adjust the amount (thickness) of the chromate film. Therefore, it is possible to arbitrarily control the thickness of the coating from thin to thick, and to obtain a coating with excellent uniformity, compared to other treatment methods, it is better to use a chromate treatment bath containing an organic resin. It is excellent despite its use. (6) In the heat treatment process after adhering the second layer chromate film, the chromium component and resin component in the second layer film, the chromium component in the first layer chromate film and the second layer resin component, respectively. By the heating polymerization reaction, it is possible to form a multilayer coating with excellent adhesion to the first layer coating simultaneously with the formation of the second layer coating. The following effects can be obtained. (Examples) In order to clarify the effects of the present invention, several examples and comparative examples will be given and specifically explained. Example 1 Electrolytic galvanized steel sheets with a plating amount of 20 g/m 2 per side were used as the material to be treated, and the plate width was
The two-layer treatment of the present invention was carried out under the conditions of 900 mm and a sheet passing speed of 90 m/min, that is, for the first layer, a chromate coating layer was provided using the chromate bath and treatment method shown in Table 1, and then the chromate coating layer was applied as shown in Table 1. The treatment of the present invention was carried out by heat treatment using the electrostatic coating apparatus shown in Table 1 and a treatment bath having the composition and properties shown in Table 1. In addition, the treatment conditions and chromate film properties of comparative examples in which the same treated materials were subjected to chromate treatment by various methods shown in Table 1 are shown. In carrying out the present invention, (1) Basic composition of the treatment bath for forming the second layer of chromate film An emulsion type acrylic resin having an average molecular weight of about 150,000 is used, and CrO 3 and Cr 6 are used as chromium components. Cr 3+ is partially reduced with alcohol, and a chromium component-containing resin solution with aluminum sulfate added as a hardening agent is used.( 2 ) Electrostatic coating method: The electrostatic coating device shown in Figure 1 is used. In addition to supplying a chromate treatment bath corresponding to the target coating amount using a metering pump and adjusting the plate threading speed and plate width,
Rotate 25,000 times at 2.0Kg/ cm2 , set the material to be treated as a positive pole and the air turbine as a negative pole, apply a voltage of 100KV during this period to negatively charge the atomized particles, and electrostatically atomized particles are charged at a constant speed. It was supplied and attached to a galvanized steel sheet. (3) Heat treatment: Heat treatment was performed at a plate temperature of 180°C for 10 seconds in a hot air oven. Using the above method, we also investigated the film performance, focusing on the effects of the treatment bath and the amount of chromate film. Table 1 shows the processing conditions according to the method of the present invention, and Table 2 shows the evaluation results of the performance characteristics of the chromate film according to the method of the present invention. The evaluation method and evaluation criteria were as follows, and the performance was compared and compared with those coated with chromate films with approximately the same amount of chromium deposited. Γ Evaluation method and evaluation criteria Treatment status and appearance After treatment and after the chromate film was formed, visual observations were made and evaluations were made using the following evaluation criteria. ◎...The chromate bath is applied uniformly to both sides during the treatment, and the chromate film formed after the heat treatment is uniformly formed without color unevenness or spot patterns.○...The chromate bath is partially applied during the treatment. The chromate film is adhered with uneven adhesion, but after heat treatment, a relatively uniform chromate film is formed. Although unevenness in the amount (thickness) of the coating is clearly observed, a chromate coating is formed on the entire surface ×...There are areas where the chromate bath is not attached due to phenomena such as running out of the processing bath or poor wetting during processing. In addition, if there are areas where no film is formed even after the chromate film is formed by heat treatment Uniform coverage of the chromate film The evaluation material is subjected to 1000 Cr characteristic Irradiate ×1000 squares, and apply Cr to each square.
Line counts (CPS) were measured. On the other hand, for the standard sample, we measured the chemical analysis value and the corresponding X-ray count number (CPS),
The microscopic chromate coverage was evaluated by determining the amount of Cr attached to each square of the evaluation material in comparison with the above measurement count number. The evaluation criteria were based on the following method, namely, the average chemical analysis value (mg/m 2 ) shown in Table 1.
◎… (within ±10%) Cr adhesion amount on the evaluation surface
If the area ratio is 85% or more of the Cr coating amount on the entire surface, ○… (within ±10%) of the Cr coating amount on the evaluation surface.
Less than 85% to 65% of the amount of Cr deposited on the entire surface
When occupying an area ratio of △... (within ±10%),
If the amount of Cr deposited on the entire surface occupies an area ratio of 65% or more, but the amount of Cr deposited (±30% or more) is present in an area ratio of 20% or more ×...The part where the amount of Cr deposit is not detected is on the evaluation surface
Corrosion resistance When present at an area ratio of 2.5% or more, (a)
Cut out a blank size of 200 x 200 mm from the flat plate (b) and the plate thickness of 0.8 mm, and cut this into a height
For each 30 mm square cylinder processed, an evaluation test was conducted for a predetermined period of time, and the evaluation was performed based on the following evaluation criteria. (a) Corrosion resistance of flat plate ◎... White rust occurrence rate less than 1% ○... White rust occurrence rate 1% or more to less than 5% △... White rust occurrence rate 5% or more to less than 20% ×... White rust occurrence rate 20% or more (b) Corrosion resistance after processing◎...White rust incidence less than 5%○...White rust occurrence rate 5% or more to less than 15%△...White rust occurrence rate 15% or more to less than 30%×...White rust occurrence rate 30% Paint adhesion After baking melamine-alkyd resin to a thickness of 25 μm, using a 0.8 mm thick evaluation material, 7 mm
Erichsen processing of height was performed. -1 Evaluation method (A) After Erichsen processing, adhere cellophane tape to the surface and peel it off, and evaluate the peeling status of the paint film using the following evaluation criteria ◎…Almost no peeling of the paint film is observed○…Approximately 1 mm diameter or less 5 points or less for paint film peeling △...More than 5 points for paint film peeling with a diameter of about 1 mm or less, or paint film peeling over a fairly large area of 10% or less of the evaluated surface ×...Large area that is clearly observed More than 10% of paint peeling occurs -2 Evaluation method (B) After immersing the painted material in boiling water for 30 minutes, drying
After being left for 24 hours, Erichsen processing was performed, and the same peeling test as above was carried out, and evaluation was made using the same criteria as above. Corrosion resistance after painting: A 25 μ thick coat of melamine-alkyd paint was applied to the evaluation material of 100 x 150 mm size. - After baking, scratches reaching the surface of the plating layer were made, and a salt spray test was conducted for a predetermined period of time to evaluate the post-painting corrosion resistance performance according to the following evaluation criteria. ◎…The maximum width of blisters from the scratch area is less than 3 mm, and no more than 3 blisters occur from other flat areas. ○...Blister width from the scratch part is less than 6 mm at most, or blisters from other flat surfaces occur in 7 points or less △...Blister width from the scratch part at maximum is less than 10 mm, or blisters occur from other flat surfaces in 10 points or less × ...If the maximum width of blisters from the scratch area is 10 mm or more, or if blisters occur from other flat areas in 11 or more cases.

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】 実施例 2 亜鉛合金メツキ鋼板、鉛及び鉛合金メツキ鋼
板、アルミ及びアルミ合金メツキ鋼板に対して、
本発明の方法によるクロメート被膜を第3表に示
す条件で形成せしめ、その被膜性能について評価
を行なつた。その結果を第4表に示す。 また、比較例としては、ほぼ同一のクロム付着
量からなるクロメート被膜を各方法で形成せしめ
たものについて、各々に対応して性能比較を行な
つた。 尚、性能評価については、以下に示す方法で行
なうとともにその評価基準に従つて、相対的に評
価を行なつた。 処理状況と処理外観 …実施例1−と同一評価を実施し、同一基
準で評価 クロメート被膜の均一被覆性 …実施例1−と同一評価を実施し、同一基
準で評価 耐食性 …実施例1−と同一評価を実施し、各評価
材の種類によつて、白錆或いは赤錆の発生率に
よつて評価を行なつた。尚、各評価材の発生率
に対する評価基準は実施例1−に準拠し、第
4表の表中に白錆又は赤錆で表示した。 塗料密着性 …実施例1−と同一評価を実施し、同一基
準で評価 塗装後耐食性 …実施例1−と同一評価を実施し、同一基
準で評価
[Table] Example 2 For zinc alloy plated steel plates, lead and lead alloy plated steel plates, aluminum and aluminum alloy plated steel plates,
A chromate film according to the method of the present invention was formed under the conditions shown in Table 3, and the film performance was evaluated. The results are shown in Table 4. As a comparative example, chromate coatings having approximately the same amount of chromium deposited were formed by each method, and the performance was compared for each method. Note that performance evaluation was performed using the method shown below, and a relative evaluation was performed according to the evaluation criteria. Processing status and appearance: The same evaluation was carried out as in Example 1-, and the same criteria were used. Uniform coverage of the chromate film: The same evaluation was carried out as in Example 1-, and the evaluation was made using the same standards. Corrosion resistance: The same evaluation was carried out as in Example 1-. The same evaluation was carried out, and the evaluation was made based on the incidence of white rust or red rust depending on the type of each evaluation material. The evaluation criteria for the occurrence rate of each evaluation material were based on Example 1-, and were indicated by white rust or red rust in Table 4. Paint adhesion...Performed the same evaluation as Example 1- and evaluated using the same standards Corrosion resistance after painting...Performed the same evaluation as Example 1- and evaluated using the same standards

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】 (発明の効果) すなわち、本発明は、金属表面処理鋼板のクロ
メート二層被膜と処理浴の相剰効果によつて、被
膜量の如何にかかわらず、均一被覆性にすぐれ、
外観性能、耐食性能、塗装性能にすぐれた高性
能、クロム含有樹脂被膜を形成する。
[Table] (Effects of the invention) In other words, the present invention has excellent uniform coverage regardless of the amount of coating due to the mutual effect of the two-layer chromate coating on the metal surface-treated steel sheet and the treatment bath.
Forms a high-performance, chromium-containing resin coating with excellent appearance, corrosion resistance, and coating performance.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は静電霧化塗布装置の説明図、第2図は
静電霧化装置の拡大説明図である。 1……塗布溶液、2……溶液タンク、3……供
給ポンプ、4……霧化装置、5……エアータービ
ン、6……表面処理鋼板、7……操作盤、8……
電気制御盤、9……高圧トランス。
FIG. 1 is an explanatory diagram of an electrostatic atomization coating device, and FIG. 2 is an enlarged explanatory diagram of the electrostatic atomization device. DESCRIPTION OF SYMBOLS 1... Coating solution, 2... Solution tank, 3... Supply pump, 4... Atomization device, 5... Air turbine, 6... Surface treated steel plate, 7... Operation panel, 8...
Electrical control panel, 9...High voltage transformer.

Claims (1)

【特許請求の範囲】[Claims] 1 金属表面処理を施した鋼板に、Cr6+を主成分
とする水溶液の電解処理法或いは塗布処理法によ
つて金属Cr換算で片面当り5〜150mg/m2のクロ
ム付着量の無機物系クロメート処理層を設け、該
クロメート被膜の上層に樹脂含有量が50〜400
g/とクロム成分がその樹脂含有量の1/50〜
1/1の比率で混合してかつ常温で粘度が3〜50
センチポアーズ、電気伝導度が2〜30ms/cmの
クロム成分含有樹脂水溶液を−80〜−100KVの
電圧を印加して毎分2万〜4万5千回で回転する
回転体に衝突させてマイナスに荷電した霧化粒子
とする静電霧化法によつて片面当りクロム付着量
を3〜180mg/m2塗布する樹脂含有クロメート処
理層を設け、加熱温度50〜350℃で加熱処理する
事を特徴とするクロメート二層被膜金属表面処理
鋼板の製造方法。
1. Inorganic chromate with a chromium deposition amount of 5 to 150 mg/m 2 per side in terms of metal Cr is applied to a steel plate that has been subjected to metal surface treatment by electrolytic treatment or coating treatment using an aqueous solution containing Cr 6+ as the main component. A treatment layer is provided, and the resin content is 50 to 400 on the upper layer of the chromate coating.
g/ and chromium component is 1/50 to 1/50 of the resin content
Mix at a ratio of 1/1 and have a viscosity of 3 to 50 at room temperature.
Centipores: Apply a voltage of -80 to -100 KV to a chromium-containing resin aqueous solution with an electrical conductivity of 2 to 30 ms/cm, and collide it with a rotating body that rotates at 20,000 to 45,000 times per minute to make it negative. A resin-containing chromate treatment layer is applied using an electrostatic atomization method using charged atomized particles to achieve a chromium deposition amount of 3 to 180 mg/ m2 per side, and is characterized by heat treatment at a heating temperature of 50 to 350°C. A method for producing a metal surface-treated steel sheet with a two-layer chromate coating.
JP24407587A 1987-09-30 1987-09-30 Production of surface-treated steel sheet having two chromate-layer coating film Granted JPS6487783A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24407587A JPS6487783A (en) 1987-09-30 1987-09-30 Production of surface-treated steel sheet having two chromate-layer coating film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24407587A JPS6487783A (en) 1987-09-30 1987-09-30 Production of surface-treated steel sheet having two chromate-layer coating film

Publications (2)

Publication Number Publication Date
JPS6487783A JPS6487783A (en) 1989-03-31
JPH0372714B2 true JPH0372714B2 (en) 1991-11-19

Family

ID=17113362

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24407587A Granted JPS6487783A (en) 1987-09-30 1987-09-30 Production of surface-treated steel sheet having two chromate-layer coating film

Country Status (1)

Country Link
JP (1) JPS6487783A (en)

Also Published As

Publication number Publication date
JPS6487783A (en) 1989-03-31

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