JPH0686677B2 - Molten salt electrolytic plating device - Google Patents
Molten salt electrolytic plating deviceInfo
- Publication number
- JPH0686677B2 JPH0686677B2 JP3918487A JP3918487A JPH0686677B2 JP H0686677 B2 JPH0686677 B2 JP H0686677B2 JP 3918487 A JP3918487 A JP 3918487A JP 3918487 A JP3918487 A JP 3918487A JP H0686677 B2 JPH0686677 B2 JP H0686677B2
- Authority
- JP
- Japan
- Prior art keywords
- molten salt
- tank
- iron
- electrolytic plating
- 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.)
- Expired - Lifetime
Links
Landscapes
- Electroplating Methods And Accessories (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は溶融塩をメツキ浴液として用いる鋼材の電解メ
ツキ装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an electrolytic plating apparatus for steel products using molten salt as a plating bath liquid.
従来より溶融塩を溶液としたアルミニウム電解メツキは
鋼材へのメツキ方法として知られているがほとんど実用
化されていない。Aluminum electrolytic plating using a molten salt as a solution has been conventionally known as a plating method for steel materials, but has not been practically used.
その理由の1つとして鋼材の表面を活性化する適当な手
段が開発されていなかつたことが挙げられるが、この問
題に対しては本出願人が先に提案した方法、すなわち、
鋼材を溶融塩電解めつきするに先立つて該鋼材に陽極溶
解処理を行い鋼材表面の活性化を図ることを特徴とする
鋼材の溶融塩電解めつき法によつて解決された〔“鋼材
の溶融塩電解めつき方法”なる表題で昭和61年12月5日
付でなした特許出願明細書参照〕。One of the reasons for this is that no suitable means for activating the surface of the steel material has been developed, but for this problem, the method previously proposed by the applicant, namely,
This was solved by the molten salt electrolytic plating method of steel, which is characterized in that the surface of the steel is activated by performing an anodic dissolution treatment on the steel prior to the electrolytic plating of the molten steel. Please refer to the specification of the patent application filed on December 5, 1986 under the heading "Salt electrolytic plating method".
しかしながら、上記提案方法には鋼材の陽極溶解により
溶融塩に溶出した鉄分は鉄イオンとなつて溶液中に蓄積
され、この鉄イオンを含んだ溶液は鋼材に付着してメツ
キ槽中の溶融塩浴液に持込まれ、メツキ浴液中の鉄イオ
ンを増加させ、メツキ溶液中の鉄イオンが増加すると鋼
材へのメツキ被膜に鉄が混入しメツキ被膜の品質を悪化
させるという問題があった。However, in the above proposed method, the iron content eluted in the molten salt by the anodic dissolution of the steel material is accumulated in the solution as iron ions, and the solution containing the iron ions adheres to the steel material and the molten salt bath in the plating tank There was a problem in that when iron particles were brought into the solution and the iron ions in the plating solution were increased, and when the iron ions in the plating solution increased, iron was mixed into the plating film on the steel and the quality of the plating film deteriorated.
そこで本出願人らは上記提案方法の欠点を解消すべく、
本発明と同日付で、溶融塩電解メツキ法をいう表題のも
とに、鋼材を溶融塩浴中で陽極溶解させ、その表面を活
性化させる前処理操作と組合せた鋼材の溶融塩電解メツ
キ方法において、鋼材の陽極溶解によつて生じた鉄イオ
ンを鉄よりもイオン化傾向の高い金属を添加混合するこ
とにより還元して金属鉄として析出させることを特徴と
する溶融塩電解メツキ方法を提案した。Therefore, in order to eliminate the drawbacks of the proposed method, the present applicants
On the same date as the present invention, under the title of molten salt electrolytic plating method, a molten salt electrolytic plating method for steel material, in which a steel material is anodically dissolved in a molten salt bath and its surface is activated, is combined with a pretreatment operation. Proposed a molten salt electrolytic plating method characterized in that iron ions produced by anodic dissolution of steel are reduced by adding and mixing a metal having a higher ionization tendency than iron to precipitate as metallic iron.
しかしながら、本発明と同日付で特許出願した上記方法
は、鋼材の陽極溶解浴液中に鉄よりもイオン化傾向の高
い金属を添加するため、該浴液中に析出した鉄が存在
し、該溶液の劣化を来たすばかりでなく、鋼材(例えば
鋼帯)搬送時には鉄が送りローラ等との間に噛み込み鋼
材表面を傷つけるという問題点を有していた。However, the above-mentioned method applied for a patent on the same date as the present invention, since a metal having a higher ionization tendency than iron is added to the anodic dissolution bath solution of the steel material, there is iron precipitated in the bath solution, In addition to the deterioration of the steel, there is a problem that the iron is caught between the feed roller and the like when the steel material (for example, the steel strip) is conveyed and the surface of the steel material is damaged.
本発明は、上記の本発明と同日付で特許出願した上記方
法における欠点を解消しうる溶融塩電解メツキ装置を提
供しようとするものである。The present invention is intended to provide a molten salt electrolytic plating apparatus capable of solving the drawbacks of the above method filed on the same date as the present invention.
本発明は、鋼材を溶融塩浴液で陽極溶解させて鋼材の表
面を活性化する前処理槽、該活性化表面処理された鋼材
にメツキする溶融塩電解メツキ槽及び前記前処理槽の浴
液と連通する鉄よりもイオン化傾向の高い金属粒を充填
した鉄イオン除去槽とよりなる溶融塩電解メツキ装置で
ある。The present invention relates to a pretreatment tank for anodic dissolution of a steel material with a molten salt bath solution to activate the surface of the steel material, a molten salt electrolytic plating tank for plating the activated surface-treated steel material, and a bath solution of the pretreatment tank. A molten salt electrolytic plating apparatus comprising an iron ion removal tank filled with metal particles having a higher ionization tendency than iron, which communicates with iron.
すなわち、本発明は、前記のように前処理槽の浴液中に
書ずる鉄イオンを外部系路によつて鉄イオン除去槽に導
き、そこで鉄よりイオン化傾向の高い金属粒子と接触さ
せて鉄を析出させるので前処理槽内の浴液を鉄によつて
劣化させることもなく、鋼材に傷つけることもなくな
る。That is, according to the present invention, as described above, the iron ions written in the bath liquid of the pretreatment tank are guided to the iron ion removal tank through an external system path, and the iron ions are brought into contact with metal particles having a higher ionization tendency than iron. Therefore, the bath liquid in the pretreatment tank is not deteriorated by iron and the steel material is not damaged.
鉄イオン除去槽で析出した鉄は例えば磁気分離器などの
手段により捕集分離除去し、鉄を除去した浴液は再び前
処理槽へもどすようにする。The iron deposited in the iron ion removal tank is collected and separated by means such as a magnetic separator, and the iron-removed bath liquid is returned to the pretreatment tank again.
本発明を鋼帯の連続溶融塩電解メツキ装置に適用した一
実施例を第1図によつて説明する。An embodiment in which the present invention is applied to a continuous molten salt electrolytic plating apparatus for steel strip will be described with reference to FIG.
第1図において、1は鋼帯、2はメツキ槽、2aは前処理
槽である陽極溶解槽、3はメツキ槽陽極板、3aは陽極溶
解槽陰極板、4はメツキ浴液、4aは陽極溶解浴液、5お
よび5aはコンダクタロール、6および6aはデフレクタロ
ール、7および7aは直流電源である(以上5〜7、5a〜
7aはaのつかない符号はメツキ槽2、aのついた符号は
前処理槽である陽極溶解槽2aにそれぞれかかわる部材を
示す)。In FIG. 1, 1 is a steel strip, 2 is a plating tank, 2a is an anode melting tank which is a pretreatment tank, 3 is a plating tank anode plate, 3a is an anode melting tank cathode plate, 4 is a plating bath liquid, and 4a is an anode. Dissolving bath liquid, 5 and 5a are conductor rolls, 6 and 6a are deflector rolls, and 7 and 7a are DC power supplies (above 5-7, 5a-
7a is a member not related to a and a member related to the plating tank 2 and a numeral to which a is related to the anode dissolving tank 2a which is a pretreatment tank).
また、8は溶融塩浴液循環回路、9はポンプ、10は鉄イ
オン除去槽であり、該鉄イオン除去槽10内には、鉄より
イオン化傾向の大きい金属(たとえばアルミニウム)粒
子の充填層11、該充填層11の粒子より目の細いスクリー
ン12、磁気分離器13、該磁気分離器13の粒子より目の細
いスクリーン14が配置されている。Further, 8 is a molten salt bath liquid circulation circuit, 9 is a pump, and 10 is an iron ion removing tank. In the iron ion removing tank 10, a packed layer 11 of metal (for example, aluminum) particles having a greater ionization tendency than iron. A screen 12 having finer mesh than the particles of the packed bed 11, a magnetic separator 13, and a screen 14 having finer mesh than the particles of the magnetic separator 13 are arranged.
第1図に示すように、鋼帯1は図示されない装置により
脱脂、酸洗水洗、乾燥処理を受けたあと、コンダクタロ
ール5aデフレクタロール6aにより、陽極溶解槽2a内陽極
溶解浴液4aに浸漬され、下降、上昇、つづいてコンダク
タロール5およびデフレクタロール6により、メツキ槽
2内のメツキ浴液4内に浸漬され、下降、上昇し、図示
されない巻取りリールに巻取られる。陽極溶解槽2aメツ
キ槽2内には鋼帯1に対面して、それぞれ陰極板3a、陽
極板3が懸吊されており、直流電源7aのプラス側はコン
ダクタロール5aに、マイナス側は陰極板3aに、また直流
電源7のプラス側は陽極板3に、マイナス側はコンダク
タロール5に接続されており、それぞれ浴液4a、4を介
して電気回路が形成されている。As shown in FIG. 1, the steel strip 1 is subjected to degreasing, pickling and rinsing and drying treatment by a device (not shown), and then immersed in the anodic dissolution bath liquid 4a in the anodic dissolution tank 2a by the conductor roll 5a and the deflector roll 6a. Then, the conductor roll 5 and the deflector roll 6 immerse it in the plating bath liquid 4 in the plating tank 2 and lowers, raises, and winds it up on a take-up reel (not shown). Anode plate 3a and anode plate 3 are suspended in the anode melting tank 2a and facing the steel strip 1 in the plating tank 2. The positive side of the DC power supply 7a is the conductor roll 5a and the negative side is the cathode plate. 3a, the positive side of the DC power source 7 is connected to the anode plate 3, and the negative side is connected to the conductor roll 5, and an electric circuit is formed via the bath solutions 4a and 4, respectively.
鋼帯1が槽2a、2に連続的に供給され、電気回路に通電
されれば、まず陽極溶解槽2a中で陽極溶解され、表面の
酸化被膜が除かれて活性化され、つづいてメツキ槽2で
メツキ処理を受け、密着性のよい良質のメツキ被膜が形
成される。If the steel strip 1 is continuously supplied to the tanks 2a and 2 and the electric circuit is energized, it is first anodically melted in the anodic melting tank 2a, the oxide film on the surface is removed and activated, and then the plating tank. In step 2, the plating process is performed to form a good quality coating film with good adhesion.
陽極溶解槽2aでは鋼帯1の表面が一旦溶解し、浴液4a中
に鉄イオンとして溶出する。このまま放置すれば、浴液
4aの中の鉄イオンが増大するので、浴液4aを外部循環回
路8を通じてポンプ9により鉄イオン除去槽10に導き、
鉄イオンを除去、浄化し、再び陽極溶解槽2aへもどす。In the anodic dissolution tank 2a, the surface of the steel strip 1 is once melted and eluted as iron ions in the bath liquid 4a. If left as it is, bath liquid
Since iron ions in 4a increase, the bath liquid 4a is guided to the iron ion removing tank 10 by the pump 9 through the external circulation circuit 8,
Iron ions are removed and purified, and then returned to the anode dissolution tank 2a again.
なお鉄イオンの除去作用について説明すれば、浴液4aを
鉄よりイオン化傾向の大きい金属粒子(たとえばアルミ
ニウム)の充填層1を通すことにより、鉄イオンは還元
されて金属鉄粉となり、そしてその金属鉄粉は磁気分離
器13により吸着捕集分離される。分離された浴液4a′は
ポンプ12を介して再び陽極溶解槽20に注入される。Explaining the iron ion removing action, the iron ions are reduced to metallic iron powder by passing the bath liquid 4a through a packed bed 1 of metal particles (for example, aluminum) having a greater ionization tendency than iron, and the metal The iron powder is adsorbed, collected and separated by the magnetic separator 13. The separated bath liquid 4a 'is reinjected into the anodic dissolution tank 20 via the pump 12.
本発明によれば、鉄イオンによる前処理槽の浴液の劣化
が防止されるのでメツキ槽へ供給される表面は十分活性
化され、密着性にすぐれた良質のメツキ被膜が安定して
形成される。According to the present invention, since the deterioration of the bath liquid of the pretreatment tank due to iron ions is prevented, the surface supplied to the plating tank is sufficiently activated, and a good quality coating film having excellent adhesion is stably formed. It
第1図は本発明を鋼帯の連続溶融塩電解メツキ方法を実
施する装置に適用した一実施例を説明するための図であ
る。FIG. 1 is a view for explaining an embodiment in which the present invention is applied to an apparatus for carrying out a continuous molten salt electrolytic plating method for steel strip.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C25F 7/02 8414−4K (72)発明者 柳 謙一 広島県広島市西区観音新町4丁目6番22号 三菱重工業株式会社広島製作所内 (72)発明者 米田 順吉 広島県広島市西区観音新町4丁目6番22号 三菱重工業株式会社広島製作所内 (72)発明者 内田 淳一 兵庫県尼崎市西長洲本通1丁目3番地 住 友金属工業株式会社総合技術研究所内 (72)発明者 瀬戸 宏久 兵庫県尼崎市西長洲本通1丁目3番地 住 友金属工業株式会社総合技術研究所内 (72)発明者 中林 寛孝 大阪府大阪市東区北浜5丁目15番地 住友 金属工業株式会社内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Reference number within the agency FI technical display location C25F 7/02 8414-4K (72) Inventor Kenichi Yanagi 4-6 Kannon Shinmachi, Nishi-ku, Hiroshima-shi, Hiroshima 22 Mitsubishi Heavy Industries Ltd. Hiroshima Works (72) Inventor Junkichi Yoneda 4-6-22 Kannon Shinmachi, Nishi-ku, Hiroshima City Hiroshima Prefecture Mitsubishi Heavy Industries Ltd. Hiroshima Works (72) Inventor Junichi Uchida Nishi Nagasumoto, Amagasaki City, Hyogo Prefecture Sumitomo Metal Industries, Ltd. General Technical Research Institute (72) Inventor Hirohisa Seto 1-3, Nishi-Nagasumoto, Amagasaki, Hyogo Prefecture Sumitomo Metal Industrial Co., Ltd. (72) Inventor Hirotaka Hayashi Sumitomo Metal Industries, Ltd. 5-15 Kitahama, Higashi-ku, Osaka-shi, Osaka
Claims (1)
表面を活性化する前処理槽、該活性化表面処理された鋼
材にメツキする溶融塩電解メツキ槽及び前記前処理槽の
浴液と連通する鉄よりもイオン化傾向の高い金属粒を充
填した鉄イオン除去槽とよりなることを特徴とする溶融
塩電解メツキ装置。1. A pretreatment tank for anodic dissolution of a steel material in a molten salt bath liquid to activate the surface of the steel material, a molten salt electrolytic plating tank for plating the activated surface-treated steel material, and a bath of the pretreatment tank. A molten salt electrolytic plating device comprising an iron ion removing tank filled with metal particles having a higher ionization tendency than iron, which is in communication with a liquid.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3918487A JPH0686677B2 (en) | 1987-02-24 | 1987-02-24 | Molten salt electrolytic plating device |
| KR1019880006732A KR910000981B1 (en) | 1986-12-05 | 1988-06-04 | Forced Molten Salt Electroplating Method and Apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3918487A JPH0686677B2 (en) | 1987-02-24 | 1987-02-24 | Molten salt electrolytic plating device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63206500A JPS63206500A (en) | 1988-08-25 |
| JPH0686677B2 true JPH0686677B2 (en) | 1994-11-02 |
Family
ID=12546026
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3918487A Expired - Lifetime JPH0686677B2 (en) | 1986-12-05 | 1987-02-24 | Molten salt electrolytic plating device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0686677B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20070110875A (en) * | 2005-03-15 | 2007-11-20 | 후지필름 가부시키가이샤 | Light-transmitting electromagnetic shielding film, optical filter and plasma television |
-
1987
- 1987-02-24 JP JP3918487A patent/JPH0686677B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63206500A (en) | 1988-08-25 |
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