JPH06235092A - Method for electrolytically chromating steel sheet excellent in color tone stability - Google Patents

Method for electrolytically chromating steel sheet excellent in color tone stability

Info

Publication number
JPH06235092A
JPH06235092A JP1992293A JP1992293A JPH06235092A JP H06235092 A JPH06235092 A JP H06235092A JP 1992293 A JP1992293 A JP 1992293A JP 1992293 A JP1992293 A JP 1992293A JP H06235092 A JPH06235092 A JP H06235092A
Authority
JP
Japan
Prior art keywords
acid
steel sheet
chromate
color tone
plating
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.)
Pending
Application number
JP1992293A
Other languages
Japanese (ja)
Inventor
Kenji Takao
研治 高尾
Chikako Kawasaki
智香子 河崎
Nobuyuki Morito
延行 森戸
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.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP1992293A priority Critical patent/JPH06235092A/en
Publication of JPH06235092A publication Critical patent/JPH06235092A/en
Pending legal-status Critical Current

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  • Electroplating Methods And Accessories (AREA)
  • Chemical Treatment Of Metals (AREA)

Abstract

PURPOSE:To stabilize the developed color tone by bringing the surface of an electrogalvanized steel sheet into contact with an acidic soln. and then electrolytically chromating the sheet. CONSTITUTION:A steel sheet having <= about 3.2mm thickness is used as the starting material. The sheet is electrogalvanized. The surface of the electrogalvanized steel sheet is brought into contact with an acidic soln. at pH 0.5-4 contg. <=1g/l of Cr<6+> ion to dissolve off the zinc oxide layer of the surface plating layer and then electrolytically chromated. An inorg. acid such as hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, boric acid and hydrofluoric acid, an org. acid such as formic acid, acetic acid and oxalic acid, a chelating material such as an EDTA soln. and an metallic salt soln. such as the solns. of ferric chloride, nickel sulfate and cobalt chloride are exemplified as the acidic soln. The steel sheet is electrolytically chromated with the color tone stabilized.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は主として家電用に使用さ
れる電解型クロメート処理電気亜鉛めっき鋼板の製造方
法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an electrolytic type chromate-treated electrogalvanized steel sheet mainly used for home appliances.

【0002】[0002]

【従来の技術】クロメート処理した電気亜鉛めっき鋼板
はその優れた耐食性および加工時に潤滑性を付与せしめ
うるため、家電用シャーシやモーターカバー等に広く用
いられている。電気亜鉛めっき鋼板上へのクロメート処
理方法としては大別して、以下の3通りの方式がある。
2. Description of the Related Art Chromate-treated electrogalvanized steel sheets are widely used for home electric appliances such as chassis and motor covers because of their excellent corrosion resistance and lubricity during processing. The chromate treatment method on the electrogalvanized steel sheet is roughly classified into the following three methods.

【0003】a)塗布型クロメート b)反応型クロメート c)電解型クロメート 塗布型クロメートは電気亜鉛めっき鋼板上へエアーナイ
フもしくはロールコータ等によってクロメート溶液を塗
布し、しかる後に水洗することなくオーブン等で焼き付
け乾燥し、クロメート皮膜を形成するものである。この
方式によると、クロメート処理液と亜鉛めっき層の反応
量が少ないため、溶出亜鉛等による処理液の劣化が少な
く、液管理が行いやすいという利点がある。しかしなが
ら、健全なクロメート皮膜を形成するためには、 100℃
以上の温度での焼き付け工程が必須になるためオーブン
が必要になり、このための設備に要するコスト高を招来
し、経済的でない。
A) Coating type chromate b) Reactive type chromate c) Electrolytic type chromate The coating type chromate is formed by applying a chromate solution onto an electrogalvanized steel sheet with an air knife or a roll coater, and then using an oven without washing with water. It is baked and dried to form a chromate film. According to this method, since the amount of reaction between the chromate treatment liquid and the zinc plating layer is small, there is an advantage that the treatment liquid is less deteriorated by eluted zinc or the like and liquid management is easy. However, in order to form a sound chromate film, 100 ℃
Since the baking process at the above temperature is indispensable, an oven is required, which causes a high cost required for equipment for this and is not economical.

【0004】第2の反応型クロメートは亜鉛めっき鋼板
を6価のCrイオンを含有した反応型クロメート溶液に浸
漬もしくはスプレー処理によって接液させ、金属亜鉛め
っき層を溶解し、同時に還元生成された3価のCrイオン
と6価のCrイオンからなるクロミュウムクロメートをゲ
ル状に析出させることにより、めっき上にクロメート皮
膜を形成せしめるものである。塗布型クロメートと異な
り、クロメート後の高温乾燥が不要のため、製造コスト
の低減が達成され、目的、用途によってさまざまなCr付
着量の反応型クロメート処理電気亜鉛めっき鋼板が製造
されている。しかしながら、皮膜形成に亜鉛めっき層の
溶解を伴うため、処理液中へのZnイオンの蓄積を余儀な
くされ、液管理が問題であるとともに、処理液の変化に
よる品質のバラツキが問題であった。さらに、化学反応
によってクロメート被膜を形成するため、付着量の制御
が困難であるという問題を内抱している。
The second reactive chromate was produced by reducing galvanized steel sheet by immersing or spraying a galvanized steel sheet in a reactive chromate solution containing hexavalent Cr ions to dissolve the metallic zinc plating layer. A chromate film is formed on the plating by precipitating a chromium chromate consisting of valent Cr ions and hexavalent Cr ions in a gel form. Unlike coating type chromate, high temperature drying after chromating is not required, so the production cost is reduced, and reactive type chromate-treated electrogalvanized steel sheets with various Cr deposits are produced depending on the purpose and application. However, since the galvanized layer is dissolved in the film formation, Zn ions are inevitably accumulated in the treatment liquid, which causes a problem in the liquid control and a variation in the quality due to the change in the treatment liquid. Furthermore, since a chromate film is formed by a chemical reaction, it has a problem that it is difficult to control the amount of adhesion.

【0005】第3の電解型クロメート処理は6価のCrイ
オンを含有したクロメート処理液中で、Zn系めっき鋼板
を陰極として電解処理することにより、クロメート皮膜
を形成するものである。この方法によると処理液中への
亜鉛の溶出が低減され、液管理が容易になるとともに、
投入電気量により付着量制御が可能になり、工業的に広
く採用されている。たとえば、耐食性を向上させるため
に処理浴中にカチオン型シリカゾルを添加する方法が特
開昭60−1108号公報に、また、陰極電解後陽極電解する
方法が特開昭62−263997号公報に開示されるなど、多く
の電解クロメートに関する技術が開示されている。
The third electrolytic chromate treatment is to form a chromate film by electrolytically treating a Zn-plated steel sheet as a cathode in a chromate treatment liquid containing hexavalent Cr ions. According to this method, the elution of zinc into the processing solution is reduced, and the solution management becomes easier,
The amount of electricity applied makes it possible to control the amount of adhesion, and is widely adopted industrially. For example, a method of adding a cationic silica sol in a treatment bath to improve corrosion resistance is disclosed in JP-A-60-1108, and a method of cathodic electrolysis followed by anodic electrolysis is disclosed in JP-A-62-263997. Many techniques relating to electrolytic chromating are disclosed.

【0006】しかしながら、これらの方法によって通常
に製造される電解クロメート鋼板は良好な耐食性および
塗装密着性は得られるものの、しばしば表面に色ムラが
生じるケースがあり、安定した外観が得られないという
問題があった。さらに、特開平3−223493号公報では酸
性浴で電解クロメートをするに先立ち、 0.5秒以上無通
電で浸漬することにより付着量の均一な電解クロメート
処理を施す方法が開示されている。この方法によると、
めっき表面の汚れや不純物が除去され、表面が均一化さ
れる。しかしながら、この際クロメート液により3価お
よび6価のクロム酸クロム(化成クロメート)が生成す
る。この化成クロメート層は、下地めっき層の状態に影
響されることが判明している。めっき層表面に酸化膜が
厚く存在すると6価クロムが多い皮膜構成になり、酸化
膜が薄く活性な状態にあるときは還元反応が進み、3価
の多い皮膜構成になる。6価と3価の比率はクロメート
の性能に影響し、特に黄色味を示す指標であるb値はこ
れにより大きく変動する。つまりこの方法によると、付
着量こそ均一ではあるが、製造チャンスにより性能、特
に色調の異なるクロメート皮膜となり、工業生産に適さ
ない。さらに、めっき表面のエッチングにより溶出した
Znイオンが蓄積され、クロメート処理の不安定性をもた
らすという不具合を生じる。
However, although electrolytic chromated steel sheets usually produced by these methods can obtain good corrosion resistance and coating adhesion, they often have uneven color on the surface, and a stable appearance cannot be obtained. was there. Further, JP-A-3-223493 discloses a method of performing electrolytic chromate treatment with a uniform amount of deposit by immersing for 0.5 seconds or more in the absence of electric current prior to electrolytic chromate treatment in an acidic bath. According to this method,
Dirt and impurities on the plating surface are removed and the surface is made uniform. However, at this time, the chromate solution produces trivalent and hexavalent chromium chromates (chemical conversion chromates). It has been found that this chemical conversion chromate layer is affected by the state of the underlying plating layer. When the oxide film is thick on the surface of the plating layer, the film structure is rich in hexavalent chromium, and when the oxide film is thin and in an active state, the reduction reaction proceeds and the film structure is highly trivalent. The ratio of hexavalent to trivalent affects the performance of chromate, and particularly the b value, which is an index showing yellowness, greatly fluctuates. In other words, according to this method, although the amount of adhesion is uniform, a chromate film having different performance, especially a color tone, is formed by a manufacturing opportunity, which is not suitable for industrial production. Furthermore, it was eluted by etching the plating surface
Zn ions are accumulated, resulting in instability of the chromate treatment.

【0007】[0007]

【発明が解決しようとする課題】本発明は上述した問題
点を解決すべくなされたもので、色調の安定した電解型
クロメート処理電気亜鉛めっき鋼板の製造方法を提供す
ることを目的とするものである。
SUMMARY OF THE INVENTION The present invention has been made to solve the above problems, and an object of the present invention is to provide a method for producing an electrolytic chromate-treated electrogalvanized steel sheet having a stable color tone. is there.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するため
に本発明によれば、電気亜鉛めっき鋼板上に電解クロメ
ート処理するに際し、めっき後かつ電解クロメート処理
前にめっき表面をpH 0.5以上4以下でかつCr6+イオン量
が1g/l以下である酸性溶液と接液することにより、
色調の安定した電気亜鉛めっき鋼板の電解クロメート処
理方法を提供することにある。
In order to achieve the above object, according to the present invention, during electrolytic chromate treatment on an electrogalvanized steel sheet, the plating surface has a pH of 0.5 or more and 4 or less after plating and before electrolytic chromate treatment. And in contact with an acidic solution having an amount of Cr 6+ ions of 1 g / l or less,
An object of the present invention is to provide a method for electrolytic chromating a galvanized steel sheet having a stable color tone.

【0009】[0009]

【作用】以下に本発明をさらに詳細に説明する。本発明
の出発原料は板厚 3.2mm以下の薄鋼板を用いる。所要の
材質を得るための熱処理を経た後、電気亜鉛めっきを施
す。電気系亜鉛めっきは一般的に工業生産に用いられる
めっき浴中で行われる。すなわちZnイオンを含有し、電
導性改善および光沢付与を目的に必要に応じて添加され
る添加剤から構成される。Znイオンの対イオンとしては
一般的に用いられる硫酸イオンであっても、塩素イオン
であってもよく、また、両者を混合した浴を用いても構
わない。
The present invention will be described in more detail below. As the starting material of the present invention, a thin steel plate having a plate thickness of 3.2 mm or less is used. After heat treatment for obtaining the required material, electrogalvanization is performed. Electrogalvanizing is generally performed in a plating bath used for industrial production. That is, it is composed of an additive that contains Zn ions and is added as needed for the purpose of improving conductivity and imparting gloss. The counter ion of Zn ion may be a generally used sulfate ion or chlorine ion, or a bath in which both are mixed may be used.

【0010】めっき槽としては、片面順次めっきである
カローセルめっき、両面同時めっきである水平セル、グ
ラビデル等の縦型セルのいずれを用いても差し支えな
い。これらのめっき槽において所定の付着量の亜鉛めっ
きが施される。本発明においてこのようにして電気亜鉛
めっきを施された鋼板は引き続き、電解型クロメート処
理が施される前にpH 0.5以上4以下の酸性溶液に接液さ
れる。
As the plating bath, any of carrousel plating which is one-sided sequential plating, horizontal cell which is simultaneously plated on both sides, and vertical type cell such as Gravidel can be used. A predetermined amount of zinc plating is applied in these plating tanks. In the present invention, the steel sheet thus electrogalvanized is subsequently brought into contact with an acidic solution having a pH of 0.5 or more and 4 or less before being subjected to electrolytic chromate treatment.

【0011】一般に製造される電解クロメート処理され
る電気亜鉛めっき鋼板はめっき後直ちに中性水でリンス
され、表面のめっき液を除去された後にドライヤーで乾
燥され、電解クロメート処理されるが、しばしば、著し
い色調ムラを生じることがあり、外観を損じていた。こ
の原因について本発明者らは鋭意研究した結果、めっき
時に形成される亜鉛の酸化物によるものであることが判
明した。以下に色調ムラの発生機構について説明する。
電気亜鉛めっき時、陰極において亜鉛イオンから金属亜
鉛への還元反応とともに水素発生が伴うため、電極界面
のpHが上昇する。このpH上昇にともなって、めっき表面
には水酸化亜鉛が推積される。この推積層は中性水によ
る水洗では除去されず、さらに80℃以上の温度でドライ
ヤーにより乾燥される過程において酸素濃淡電池による
腐食のため酸化亜鉛が生成する。このような表面状態の
めっき上に電解によるクロメートを施すと、亜鉛酸化物
が付着した部分と金属亜鉛が露出している部分において
電極反応性に差異が生じ、これが色調ムラの原因になる
ものである。
[0011] Generally, electrolytic chromate-treated electrogalvanized steel sheets produced are rinsed with neutral water immediately after plating to remove the plating solution on the surface, dried with a drier, and electrolytic chromate-treated, but often, There was a case where remarkable color unevenness was generated, and the appearance was impaired. As a result of diligent research conducted by the present inventors on this cause, it has been found that it is due to the oxide of zinc formed during plating. The mechanism of occurrence of uneven color tone will be described below.
During electrogalvanizing, the pH of the electrode interface rises because hydrogen is generated along with the reduction reaction of zinc ions to metallic zinc at the cathode. With this increase in pH, zinc hydroxide is deposited on the plating surface. This thrust layer is not removed by washing with neutral water, and zinc oxide is generated due to corrosion by the oxygen concentration battery in the process of drying with a dryer at a temperature of 80 ° C or higher. When electrochromic chromate is applied to plating with such a surface condition, there is a difference in electrode reactivity between the area where zinc oxide is attached and the area where metallic zinc is exposed, which causes uneven color tone. is there.

【0012】本発明者らは電解クロメート処理鋼板の色
ムラ改善を目的として、かかるめっき表面上の亜鉛酸化
物を除去する方法についてさらに鋭意検討した結果、め
っき後の鋼板とpH 0.5以上4以下でかつCr6+イオン量が
1g/l以下である酸性溶液と接液せしめる方法が有効
であることを見いだし、本発明に至ったものである。本
発明に用いられる酸性溶液としては塩酸、硫酸、硝酸、
リン酸、ほう酸、弗酸等の無機酸、ギ酸、酢酸、シュウ
酸等の有機酸、EDTA溶液等のキレート剤、第2塩化
鉄、硫酸ニッケル、塩化コバルト溶液等の金属塩溶液等
が挙げられ、これらを単独もしくは複合添加して用いる
ことができる。
The inventors of the present invention have made further studies as to a method for removing zinc oxide on the plated surface for the purpose of improving the color unevenness of the electrolytic chromate-treated steel sheet. Further, they have found that the method of bringing the solution into contact with an acidic solution having an amount of Cr 6+ ions of 1 g / l or less is effective, and arrived at the present invention. The acidic solution used in the present invention includes hydrochloric acid, sulfuric acid, nitric acid,
Inorganic acids such as phosphoric acid, boric acid and hydrofluoric acid, organic acids such as formic acid, acetic acid and oxalic acid, chelating agents such as EDTA solution, metal salt solutions such as ferric chloride, nickel sulfate and cobalt chloride solution. These can be used alone or in combination.

【0013】ここで亜鉛よりも電気化学的に貴な金属塩
を用いると、めっき上に金属が置換析出するが、本発明
においてはかかる金属の析出を目的とするものではな
く、酸化物の除去が目的である。必要以上に接液するこ
とによって、金属が析出して亜鉛めっき上を被覆する
と、かえって電解クロメート時の電極反応を阻害するの
で望ましくない。
When a metal salt which is more electrochemically noble than zinc is used here, the metal is deposited by substitution on the plating. However, the present invention is not intended to deposit such a metal and removes the oxide. Is the purpose. It is not desirable that the metal deposits on the zinc plating by contacting it with liquid more than necessary and the electrode reaction during electrolytic chromate is rather hindered.

【0014】また、リン酸系の溶液を使用すると、めっ
き上にリン酸塩皮膜が形成され、同じく必要以上の接液
は望ましくない。いずれについても注意が肝要である。
これらの酸性溶液に接液する方法としては浸漬処理、ス
プレー処理いずれの方法によってもよい。必ずしも特別
な設備が必要な訳でなく、例えば酸性めっき処理浴中で
めっき後無通電の状態で数秒曝しておくことも可能であ
る。
When a phosphoric acid-based solution is used, a phosphate film is formed on the plating, and excessive contact with liquid is also undesirable. Attention is necessary in any case.
The method of contacting these acidic solutions may be either dipping treatment or spraying treatment. It is not always necessary to use special equipment, and it is possible, for example, to carry out exposure for several seconds in a non-energized state after plating in an acidic plating treatment bath.

【0015】本発明において使用する酸性液はpH 0.5以
上4以下である。pH 0.5未満の如き強酸においては、め
っき層表層のみならずめっき層自体が著しく溶解し不適
であるからであり、pH4超であるとめっき表層の亜鉛酸
化層を溶解除去するに十分でないためである。pH 0.5以
上4以下の範囲、望ましくはpH 0.8〜2の範囲におい
て、本発明の効果が十分発揮される。
The acidic liquid used in the present invention has a pH of 0.5 or more and 4 or less. This is because a strong acid having a pH of less than 0.5 is not suitable because not only the plating layer surface layer but also the plating layer itself is remarkably dissolved, and if the pH exceeds 4 it is not sufficient to dissolve and remove the zinc oxide layer of the plating surface layer. . The effects of the present invention are sufficiently exhibited in the range of pH 0.5 or more and 4 or less, preferably in the range of pH 0.8 to 2.

【0016】また、酸性液中に含有されるCr6+量は1g
/l以下に限定される。1g/lを超えてCr6+が含有さ
れると、上述したように下地に化成クロメート層が形成
され、性能、特に色調が不安定になるためである。酸性
溶液の温度および接液時間は上述したように使用する溶
液種類によって異なるので、特に限定するものではない
が、めっき上の亜鉛酸化物が十分除去でき、かつ必要以
上にめっき層自体を溶解することなく、また不必要な金
属等の被覆がなされないようになされねばならない。こ
の観点から酸性溶液の温度としては20〜80℃、接液時間
として 0.1〜30秒が好ましい。
The amount of Cr 6+ contained in the acidic liquid is 1 g.
/ L or less. This is because if Cr 6+ is contained in an amount of more than 1 g / l, the chemical conversion chromate layer is formed on the underlayer as described above, and the performance, especially the color tone becomes unstable. The temperature of the acidic solution and the liquid contact time are not particularly limited because they vary depending on the type of solution used as described above, but zinc oxide on the plating can be sufficiently removed and the plating layer itself is unnecessarily dissolved. It must be done without any unnecessary coating of metal or the like. From this viewpoint, the temperature of the acidic solution is preferably 20 to 80 ° C., and the liquid contact time is preferably 0.1 to 30 seconds.

【0017】酸性溶液に接液後電解クロメート処理する
までの間において、必要に応じて水洗・乾燥を行っても
よいが、上述したように乾燥温度が80℃以上の高温にな
ると、亜鉛酸化物が形成される場合があり好ましくな
い。電解クロメート処理としては陰極電解処理によりめ
っき上にクロメート皮膜を形成するものであれば、特に
限定するものではない。通常6価のクロム酸を主成分と
し、必要に応じてZn、Ni、Co等の金属イオン、塩化物イ
オン、硫酸塩イオン、硝酸イオン等のアニオン、シリカ
ゾル、アルミナゾル等の無機酸、有機樹脂等が添加され
る。
If necessary, washing and drying may be carried out after the contact with the acidic solution and before the electrolytic chromate treatment. However, as described above, when the drying temperature reaches a high temperature of 80 ° C. or higher, zinc oxide is used. May be formed, which is not preferable. The electrolytic chromate treatment is not particularly limited as long as it forms a chromate film on the plating by cathodic electrolysis treatment. Usually, hexavalent chromic acid is the main component, and if necessary, metal ions such as Zn, Ni and Co, anions such as chloride ions, sulfate ions, nitrate ions, inorganic acids such as silica sol and alumina sol, organic resins, etc. Is added.

【0018】以下、本発明を実施例に基づいてより具体
的に説明する。
Hereinafter, the present invention will be described more specifically based on examples.

【0019】[0019]

【実施例】【Example】

実施例1 素材として、板厚 0.7mmの冷延鋼板SPCCを用いた。
電気亜鉛めつきとしては、以下のめっき浴で、白金を対
極とした流動層セルを使用して行った。 めっき浴; ZnSO4・7H2O 430g/l K2SO4 2g/l Na2SO4 4g/l pH 1.5 (H2SO4で調整) 浴温 60℃ 工程は、電解脱脂→5%硫酸酸洗→電気めっき→水洗1
→乾燥1→酸性液処理→水洗2→乾燥2→電解クロメー
トの順であり、酸性液処理は表1に示す酸性液を用い、
表2に示す条件で処理を行った。
Example 1 A cold rolled steel plate SPCC having a plate thickness of 0.7 mm was used as a material.
Electroplating with zinc was carried out in the following plating bath using a fluidized bed cell with platinum as the counter electrode. Plating bath; ZnSO 4 / 7H 2 O 430 g / l K 2 SO 4 2 g / l Na 2 SO 4 4 g / l pH 1.5 (adjusted with H 2 SO 4 ) Bath temperature 60 ° C Electrolytic degreasing → 5% sulfuric acid Washing → Electroplating → Washing 1
→ Dry 1 → Acidic solution treatment → Washing 2 → Drying 2 → Electrolytic chromate, in order, using the acidic solution shown in Table 1,
The treatment was performed under the conditions shown in Table 2.

【0020】電気亜鉛めっきの電流密度は 100A/dm2
で付着量として20g/m2 になるよう行った。電解クロ
メート処理はCrO3を50g/l、 Na3SiF5を1g/l、カ
チオン型シリカゾル{日産化学(株)社製、商品名:ス
ノーテックスAK}をSiO2として8g/l含む60℃の液
で10A/dm2 、10C/dm2 の電解条件で行った。電解ク
ロメート処理後直ちに水洗を行い、ドライヤーで乾燥し
た。
The current density of electrogalvanizing is 100 A / dm 2
The coating amount was 20 g / m 2 . The electrolytic chromate treatment includes CrO 3 50 g / l, Na 3 SiF 5 1 g / l, cationic silica sol {Nissan Chemical Co., Ltd., trade name: Snowtex AK} 8 g / l as SiO 2 at 60 ° C. The solution was electrolyzed under the conditions of 10 A / dm 2 and 10 C / dm 2 . Immediately after the electrolytic chromate treatment, it was washed with water and dried with a dryer.

【0021】クロメート処理後の外観はサンプルの任意
10点について色差測定(日本電色工業社製TC−180
0 SZ−Σ80型)を行い、黄色味の指標であるb値
を測定した。外観の色ムラの判定としてb値の標準偏差
σを算出して、以下のように評価を行った。 σ≦0.5 : ◎ 0.5<σ≦1.0 : ○ 1.0<σ≦3.0 : △ 3.0<σ : × 結果を表2に示した。
Appearance after chromate treatment is optional for sample
Color difference measurement for 10 points (TC-180 manufactured by Nippon Denshoku Industries Co., Ltd.)
0 SZ-Σ80 type) and the b value, which is an index of yellowness, was measured. The standard deviation σ of the b value was calculated to determine the color unevenness of the appearance, and the evaluation was performed as follows. σ ≦ 0.5: ◎ 0.5 <σ ≦ 1.0: ○ 1.0 <σ ≦ 3.0: Δ3.0 <σ: × The results are shown in Table 2.

【0022】[0022]

【表1】 [Table 1]

【0023】[0023]

【表2】 [Table 2]

【0024】表から明らかなように本発明例のクロメー
ト処理電気亜鉛めっき鋼板はいずれも安定した色調を示
す。
As is apparent from the table, all the chromate-treated electrogalvanized steel sheets of the present invention show a stable color tone.

【0025】[0025]

【発明の効果】本発明は以上説明したように構成されて
いるので、本発明の電気亜鉛めっき鋼板の電解クロメー
ト処理方法は色調の安定したものを容易に製造すること
ができ、工業的に広く利用することができる。
Since the present invention is constructed as described above, the electrolytic chromate treatment method for electrogalvanized steel sheet of the present invention can easily produce a product having a stable color tone, and is industrially widely used. Can be used.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 電気亜鉛めっき鋼板上に電解クロメート
処理するに際し、めっき後かつ電解クロメート処理前に
めっき表面をpH 0.5以上4以下でかつCr6+イオン量が1
g/l以下である酸性溶液と接液することを特徴とする
色調の安定した電気亜鉛めっき鋼板の電解クロメート処
理方法。
1. When electrolytically chromating a galvanized steel sheet, the plating surface has a pH of 0.5 to 4 and a Cr 6+ ion amount of 1 after plating and before electrolytic chromate treatment.
A method for electrolytic chromate treatment of an electrogalvanized steel sheet having a stable color tone, which comprises contacting with an acidic solution of g / l or less.
JP1992293A 1993-02-08 1993-02-08 Method for electrolytically chromating steel sheet excellent in color tone stability Pending JPH06235092A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1992293A JPH06235092A (en) 1993-02-08 1993-02-08 Method for electrolytically chromating steel sheet excellent in color tone stability

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1992293A JPH06235092A (en) 1993-02-08 1993-02-08 Method for electrolytically chromating steel sheet excellent in color tone stability

Publications (1)

Publication Number Publication Date
JPH06235092A true JPH06235092A (en) 1994-08-23

Family

ID=12012718

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1992293A Pending JPH06235092A (en) 1993-02-08 1993-02-08 Method for electrolytically chromating steel sheet excellent in color tone stability

Country Status (1)

Country Link
JP (1) JPH06235092A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT500839B1 (en) * 2005-02-14 2006-04-15 Hinke Schwimmbad Oesterreich G Marking colored lines on a stainless steel swimming pool comprises electrodepositing a colored layer from a electrolyte dispensed from a moving applicator
CN103510129A (en) * 2013-09-23 2014-01-15 中国人民解放军装甲兵工程学院 Ni-Co-X chromium-substituting electric brush plating solution

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT500839B1 (en) * 2005-02-14 2006-04-15 Hinke Schwimmbad Oesterreich G Marking colored lines on a stainless steel swimming pool comprises electrodepositing a colored layer from a electrolyte dispensed from a moving applicator
CN103510129A (en) * 2013-09-23 2014-01-15 中国人民解放军装甲兵工程学院 Ni-Co-X chromium-substituting electric brush plating solution
CN103510129B (en) * 2013-09-23 2016-03-09 中国人民解放军装甲兵工程学院 A kind of Ni-Co-X is for chromium electric brush plating liquor

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