JP3038249B2 - Anodizing treatment method for metal surface - Google Patents

Anodizing treatment method for metal surface

Info

Publication number
JP3038249B2
JP3038249B2 JP3076015A JP7601591A JP3038249B2 JP 3038249 B2 JP3038249 B2 JP 3038249B2 JP 3076015 A JP3076015 A JP 3076015A JP 7601591 A JP7601591 A JP 7601591A JP 3038249 B2 JP3038249 B2 JP 3038249B2
Authority
JP
Japan
Prior art keywords
aqueous solution
treatment
acid
anodic dissolution
electrolytic
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
Application number
JP3076015A
Other languages
Japanese (ja)
Other versions
JPH04311598A (en
Inventor
義明 井田
文幸 津高
英貴 上田
惠吾 小幡
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.)
MARUI GALVANIZING CO., LTD
Original Assignee
MARUI GALVANIZING CO., LTD
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 MARUI GALVANIZING CO., LTD filed Critical MARUI GALVANIZING CO., LTD
Priority to JP3076015A priority Critical patent/JP3038249B2/en
Publication of JPH04311598A publication Critical patent/JPH04311598A/en
Application granted granted Critical
Publication of JP3038249B2 publication Critical patent/JP3038249B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
  • Electroplating Methods And Accessories (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明はステンレス鋼、あるいは
銅、黄銅、青銅等の銅合金等の金属表面の陽極溶解処理
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 anodic dissolution treatment of a metal surface such as stainless steel or a copper alloy such as copper, brass or bronze.

【0002】[0002]

【従来の技術】例えば、溶接、溶断等によって局部的に
加熱された例えばステンレス鋼等の合金鋼や、ロウ付け
等の際の加熱されたり長時間の空気中で放置された銅や
その合金の表面には酸化物(スケール)が生成されて、
表面の光沢が失われて美観を損ねたり、該酸化物の生成
箇所から腐食を生じることがある。このような金属の表
面に生成された酸化物を除去する方法のひとつに、陽極
溶解処理が行われている。
2. Description of the Related Art For example, alloy steel such as stainless steel locally heated by welding, fusing, or the like, or copper or an alloy thereof heated during brazing or left in air for a long time. Oxide (scale) is generated on the surface,
The gloss of the surface may be lost and the aesthetic appearance may be impaired, or corrosion may occur from the formation site of the oxide. An anodic dissolution treatment is performed as one of the methods for removing oxides generated on the surface of such a metal.

【0003】また金属表面の研磨やバリ取り、さらには
例えばネームプレート、銘板製作のためのエッチング処
理としても機械的研磨や酸洗い等に代わって上記陽極溶
解処理が適用される場合がある。この陽極溶解処理とし
ては、陽極に接続された被処理金属を陰極に接続された
電極片とともに槽中に満たした電解液中に浸漬して電解
処理が行われる浸漬法と、陽極に接続された被処理金属
の表面を、電解液を含浸したフェルト、スポンジ等の滞
水性材料で被覆された陰極に接続された処理筆具で通電
しながら払拭するブラシ法とがある。
The above-mentioned anodic dissolution treatment may be applied instead of mechanical polishing, pickling, etc., for polishing or deburring a metal surface, and for example, also for etching treatment for producing a name plate or a nameplate. As the anodic dissolution treatment, an immersion method in which the metal to be treated connected to the anode was immersed in an electrolytic solution filled in a tank together with an electrode piece connected to the cathode to perform an electrolytic treatment, and the anode was connected to the anode. There is a brush method in which the surface of the metal to be treated is wiped while energizing the surface with a treatment brush connected to a cathode coated with a water-repellent material such as felt or sponge impregnated with an electrolytic solution.

【0004】上記浸漬法に用いられる電解液としては硫
酸、塩酸、硝酸、フッ酸、リン酸等から選ばれる1種も
しくは2種以上の強酸の水溶液が採用される一方、ブラ
シ法は上記浸漬法と異なり処理従事者も表面処理の専門
技術者でないことから、例えば特公平1−27160号
公報に記載の合金鋼の脱スケール法においては電解液と
して、より安全で衛生的なリン酸のナトリウム塩、カリ
ウム塩、アンモニウム塩の単独水溶液、もしくは硫酸、
硝酸、フッ酸のナトリウム塩、カリウム塩、アンモニウ
ム塩との混合水溶液とグリセリンとの混合水溶液を採用
して、上記浸漬法で採用されたような取扱や装置等に特
別の配慮や装置を不要とする陽極溶解処理方法が開示さ
れている。
The electrolytic solution used in the immersion method is an aqueous solution of one or more strong acids selected from sulfuric acid, hydrochloric acid, nitric acid, hydrofluoric acid, phosphoric acid and the like, while the brush method is an immersion method. Unlike the surface treatment workers, which are not specialists in surface treatment, for example, in the descaling method of alloy steel described in Japanese Patent Publication No. 1-27160, a safer and more sanitary sodium salt of phosphoric acid is used as an electrolyte. , Potassium salt, aqueous solution of ammonium salt alone or sulfuric acid,
By using a mixed aqueous solution of sodium, potassium and ammonium salts of nitric acid and hydrofluoric acid and a mixed aqueous solution of glycerin, special handling and equipment such as those used in the above immersion method are not required. An anodic dissolution treatment method is disclosed.

【0005】[0005]

【発明が解決しようとする課題】ところでこのような陽
極溶解処理方法において、被処理金属の処理面の仕上が
り状態や処理速度の遅速は電解液の成分が重要な要因を
占めている。特にブラシ法においては被処理部の周辺付
近の仕上がりムラむらが少ないことが求められる。しか
しながら、上記特公平1−27160号公報に記載の発
明では、浸漬法において強酸を電解液として処理を行う
方法に比べて処理速度で劣り、また被処理部の周辺付近
の仕上がりムラを生じることが指摘されている。こうし
た欠点は上記浸漬法における電解液としての硫酸、塩
酸、硝酸、フッ酸、リン酸等の強酸単独水溶液に比べて
反応性に劣る正リン酸の使用したことによるものと考え
られる。
In such an anodic melting treatment method, the finished state of the treated surface of the metal to be treated and the slowing of the treating speed are determined by the components of the electrolytic solution. In particular, in the brush method, it is required that there is little unevenness in finish near the periphery of the portion to be processed. However, in the invention described in Japanese Patent Publication No. 27160/1990, the immersion method is inferior in the processing speed as compared with the method in which a strong acid is used as an electrolytic solution, and may cause unevenness in the finish in the vicinity of the portion to be processed. It is pointed out. It is considered that such a drawback is caused by the use of orthophosphoric acid, which is inferior in reactivity to an aqueous solution of a strong acid such as sulfuric acid, hydrochloric acid, nitric acid, hydrofluoric acid, phosphoric acid, etc., as an electrolytic solution in the immersion method.

【0006】本発明は上記従来の事情に鑑み提案された
ものであって、取扱が容易でありながら、美麗な仕上が
り状態となり、処理時間の短縮を実現した金属表面の陽
極溶解処理方法を提供することを目的とするものであ
る。
The present invention has been proposed in view of the above-mentioned conventional circumstances, and provides an anodic dissolving method for a metal surface which is easy to handle, has a beautiful finished state, and has a reduced processing time. The purpose is to do so.

【0007】[0007]

【課題を解決するための手段】上記の目的を達成するた
めに本発明は以下の手段を採用する。すなわち、金属表
面の陽極溶解処理方法において、ピロリン酸のカリウム
塩、アンモニウム塩のいずれか、あるいは両方を含有す
る水溶液、もしくはポリリン酸水溶液を電解液とし、被
処理金属を陽極に接続して直流で電解処理を行うか、も
しくは被処理金属に直流電源の陽極に接続して該直流に
交流を重畳させた電流で電解処理を行う構成とする。
In order to achieve the above object, the present invention employs the following means. That is, in the anodic dissolution treatment method for the metal surface, an aqueous solution containing either or both of potassium phosphate and ammonium salt of pyrophosphoric acid, or an aqueous solution of polyphosphoric acid is used as an electrolytic solution. Either electrolytic treatment is performed, or electrolytic treatment is performed with a current in which an alternating current is superimposed on the direct current by connecting the treated metal to the anode of a direct current power supply.

【0008】[0008]

【作 用】上記の構成において採用するポリリン酸と
は、正リン酸よりも反応性に優る縮合リン酸の総称であ
り、鎖状のピロリン酸、トリリン酸、テトラリン酸なら
びに環状の縮合リン酸であるトリメタリン酸、テトラメ
タリン酸等を包含する物質を指し、このような縮合リン
酸を電解液の構成成分として採用することにより電解処
理時の反応性を向上させて、美麗にかつ、短い処理時間
で処理を行うことができる。
[Function] The polyphosphoric acid used in the above constitution is a general term for condensed phosphoric acid which is more reactive than orthophosphoric acid, and includes chain pyrophosphoric acid, triphosphoric acid, tetraphosphoric acid and cyclic condensed phosphoric acid. Refers to a substance containing trimetaphosphoric acid, tetrametaphosphoric acid, etc., and improves the reactivity at the time of electrolytic treatment by adopting such condensed phosphoric acid as a component of the electrolytic solution, so that the treatment time is beautiful and short. Can be performed.

【0009】上記電解液としての水溶液に含有されるピ
ロリン酸のカリウム塩、アンモニウム塩のいずれか、あ
るいは両方を含有する水溶液の濃度は10〜50重量%
の範囲が望ましく、10重量%未満では望ましい処理時
間内に陽極溶解を行うことができず、50重量%を超え
る場合には上記ピロリン酸のカリウム塩、アンモニウム
塩の溶解度が飽和状態に達するため電解液としての使用
に耐えなくなる。また上記電解液としてポリリン酸水溶
液を採用する場合にはその濃度が10重量%以上とする
ことが望ましく、10重量%未満の濃度では望ましい処
理時間内に陽極溶解を行うことができなくなる恐れがあ
り好ましくない。
The concentration of the aqueous solution containing either or both of the potassium salt and the ammonium salt of pyrophosphoric acid contained in the aqueous solution as the electrolytic solution is 10 to 50% by weight.
If the amount is less than 10% by weight, anodic dissolution cannot be performed within a desired treatment time, and if it exceeds 50% by weight, the solubility of the potassium and ammonium salts of pyrophosphoric acid reaches a saturated state. It cannot withstand use as a liquid. When an aqueous solution of polyphosphoric acid is used as the electrolyte, the concentration is preferably 10% by weight or more, and if the concentration is less than 10% by weight, anodic dissolution may not be performed within a desired processing time. Not preferred.

【0010】さらに、上記ピロリン酸のカリウム塩、ア
ンモニウム塩のいずれか、あるいは両方を含有する水溶
液を電解液とする場合にはpHを9.5以下とすること
が望ましく、該pHが9.5を超える場合には上記ピロ
リン酸のカリウム塩、アンモニウム塩が電解液中に結晶
となって析出することがあり好ましくない。特にピロリ
ン酸のカリウム塩の単独溶液は加水分解によりpH10
前後の強アルカリ性を呈するところから、上記の傾向が
顕著であることに加えて、例えばブラシ法においてはこ
のような強アルカリ液の取扱に伴う煩瑣な注意を不要と
するために、例えばリン酸(特に縮合リン酸である必要
はない)などのpH調整剤を添加して、該pHを低下さ
せることが望ましい。
Further, when an aqueous solution containing either or both of the potassium salt and the ammonium salt of pyrophosphoric acid is used as the electrolytic solution, the pH is desirably 9.5 or less, and the pH is 9.5 or less. In the case of exceeding the above, the potassium and ammonium salts of pyrophosphoric acid are not preferable because they may precipitate as crystals in the electrolytic solution. In particular, a single solution of a potassium salt of pyrophosphoric acid has a pH of 10 due to hydrolysis.
In view of the strong alkaline property before and after, in addition to the above-mentioned tendency being remarkable, for example, in the brush method, in order to eliminate the need for complicated handling of such a strong alkaline solution, for example, phosphoric acid ( It is preferable to lower the pH by adding a pH adjuster such as condensed phosphoric acid.

【0011】尚、本発明においては陽極溶解処理による
処理箇所の仕上がり状態を向上させるための種々の物質
を添加することを何ら妨げるものではない。このような
電解液を用いて陽極溶解処理を行う際には直流だけを通
電しても良いが、特にステンレス鋼のスケール除去処理
を行う際には、該ステンレス鋼を長時間にわたって高い
電位状態とすると、表面が不働態化して処理時間が長く
かかることが知られており、上記直流に該直流よりも若
干高い値の最高電圧とした交流を重畳させて一時的に負
の電位として該陽極溶解処理を促進することも行うこと
ができる。
In the present invention, the addition of various substances for improving the finished state of the treated portion by the anodic dissolution treatment is not hindered at all. When performing anodic dissolution treatment using such an electrolytic solution, only a direct current may be applied, but particularly when performing scale removal treatment of stainless steel, the stainless steel is kept in a high potential state for a long time. Then, it is known that the surface is passivated and a long processing time is required. The direct current is superimposed on the direct current with an alternating current having a maximum voltage slightly higher than the direct current, and temporarily becomes a negative potential to dissolve the anode. Processing can also be facilitated.

【0012】[0012]

【実施例】以下、本発明を適用した実施例につき説明
し、その効果を検証する。 =実施例1= ピロリン酸カリウム100g/lからなる水溶液にリン
酸を添加し、pHを9.0に調整した電解液中に、陽極
に接続したろう付けを施した箇所のある黄銅サンプルを
浸漬し、6A/dm2 の電流密度の直流で陽極溶解処理
を施した。処理時間約60秒で極めて美麗な表面をもつ
黄銅サンプルが得られた。
Embodiments of the present invention will be described below to verify the effects. = Example 1 = A brass sample with a brazed part connected to the anode was immersed in an electrolytic solution adjusted to pH 9.0 by adding phosphoric acid to an aqueous solution composed of potassium pyrophosphate 100 g / l. Then, an anodic dissolution treatment was performed with a direct current having a current density of 6 A / dm 2 . A brass sample having a very beautiful surface was obtained with a treatment time of about 60 seconds.

【0013】一方、比較対照区として硫酸ナトリウム1
00g/lの水溶液を電解液として、上記と同様の処理
条件で陽極溶解処理を行ったところ、明瞭な素地荒れが
見られた。 =実施例2= ピロリン酸カリウム350g/lからなる水溶液にリン
酸を添加し、pHを8.0に調整した電解液中に、陽極
に接続した溶接箇所を有するSUS304ステンレス鋼を浸漬
し、200A/dm2 の電流密度の直流で陽極溶解処理
を施した。処理時間約60秒で極めて美麗に溶接焼けを
除去できた。
On the other hand, sodium sulfate 1
When the anodic dissolution treatment was performed under the same treatment conditions as above using an aqueous solution of 00 g / l as an electrolyte, a clear roughening of the substrate was observed. = Example 2 = SUS304 stainless steel having a welded part connected to the anode was immersed in an electrolytic solution adjusted to pH 8.0 by adding phosphoric acid to an aqueous solution containing 350 g / l of potassium pyrophosphate, and subjected to 200 A The anodic dissolution treatment was performed with a direct current having a current density of / dm 2 . In about 60 seconds, the burn was successfully removed.

【0014】一方、比較対照区として硫酸ナトリウム2
00g/lの水溶液を電解液として、上記と同様の処理
条件で陽極溶解処理を行ったところ、スケール除去に長
時間を要したことに加えて、明瞭な素地荒れが見られ
た。=実施例3=ピロリン酸340g/lからなる水溶
液にアンモニア水を添加し、pHを3.5に調整したピ
ロリン酸アンモニウム溶液を電解液として、電極表面を
被覆するフェルトに含浸させた。この後該電極を陰極に
接続する一方、自然放置によって褐色に変色した銅板を
陽極に接続して電圧6Vの直流電流を通電するブラシ法
による陽極溶解処理を行った。処理時間約60秒で極め
て美麗に仕上がりで光沢を回復した銅板が得られた。
On the other hand, sodium sulfate 2
When the anodic dissolution treatment was carried out under the same treatment conditions as above using an aqueous solution of 00 g / l as an electrolytic solution, it took a long time to remove the scale, and a clear roughening was observed. Example 3 Ammonia water was added to an aqueous solution containing 340 g / l of pyrophosphoric acid, and an ammonium pyrophosphate solution whose pH was adjusted to 3.5 was used as an electrolytic solution to impregnate a felt covering the electrode surface. Thereafter, while the electrode was connected to the cathode, a copper plate turned brown by natural standing was connected to the anode, and an anode dissolution treatment was performed by a brush method in which a DC current of 6 V was applied. With a processing time of about 60 seconds, a copper plate having a very beautiful finish and a restored gloss was obtained.

【0015】=実施例4= ピロリン酸カリウム350g/lからなる水溶液にリン
酸を添加し、pHを4.5に調整した電解液中に、陽極
に接続したエメリペーパーで微細な疵を付けた黄銅片を
浸漬し、10A/dm2 の電流密度の直流で陽極溶解処
理を施した。処理時間約30秒で極めて美麗な光沢を取
り戻した黄銅片が得られた。
= Example 4 = Phosphoric acid was added to an aqueous solution consisting of 350 g / l of potassium pyrophosphate, and fine scratches were made with an emery paper connected to the anode in an electrolytic solution adjusted to pH 4.5. The brass pieces were immersed and subjected to anodic dissolution treatment with a direct current having a current density of 10 A / dm 2 . A brass piece having a very beautiful luster was obtained in a processing time of about 30 seconds.

【0016】=実施例5= ピロリン酸カリウム400g/lからなる水溶液にリン
酸を添加し、pHを7.5に調整した水溶液を電解液と
して、電極表面を被覆するフェルトに含浸させた。この
後、該電極を陰極に接続する一方、溶接箇所を有するSU
S304ステンレス鋼を陽極に接続し、電圧25Vの直流電
流を通電させるとともに、該直流電流に最高電圧30
V、周波数60Hzの交流電流を重畳させて電解処理を
行うブラシ法による陽極溶解処理を施したところ、処理
時間約20秒で極めて美麗に溶接焼けを除去できた。
Example 5 Phosphoric acid was added to an aqueous solution composed of 400 g / l of potassium pyrophosphate, and an aqueous solution whose pH was adjusted to 7.5 was used as an electrolytic solution to impregnate a felt covering the electrode surface. Thereafter, while the electrode is connected to the cathode, the SU
S304 stainless steel was connected to the anode, a DC current of 25 V was applied, and a maximum voltage of 30 V was applied to the DC current.
When the anodic dissolution treatment was performed by a brush method in which an alternating current of V and a frequency of 60 Hz was superimposed and the electrolytic treatment was performed, welding scorch could be removed very beautifully in a treatment time of about 20 seconds.

【0017】一方対照区として、硫酸アンモニウム20
0g/lの水溶液を電解液として上記と同様の処理を行
ったところ、処理過程においてアンモニアによる刺激臭
が強く発生して、スケール除去に長時間を要したのみな
らず、明瞭な素地荒れが見られた。 =実施例6= ポリリン酸4容量部、水10容量部よりなる混合液を、
電極表面を被覆するフェルトに含浸させた。この後、該
電極を陰極に接続する一方、溶接箇所を有するSUS304ス
テンレス鋼を陽極に接続し、電圧25Vの直流を通電し
て電解処理を行うブラシ法による陽極溶解処理を施した
ところ、処理時間約60秒で極めて美麗に溶接焼けを除
去できた。
On the other hand, as a control, ammonium sulfate 20
When the same treatment as above was performed using an aqueous solution of 0 g / l as an electrolytic solution, a strong irritating smell due to ammonia was generated in the treatment process, not only it took a long time to remove the scale, but also a clear roughening was observed. Was done. = Example 6 = A mixed solution consisting of 4 parts by volume of polyphosphoric acid and 10 parts by volume of water
The felt covering the electrode surface was impregnated. Thereafter, while the electrode was connected to the cathode, SUS304 stainless steel having a welded portion was connected to the anode, and a current of 25 V was applied with a direct current to perform anodic dissolution treatment by a brush method in which electrolytic treatment was performed. In about 60 seconds, the welding burn was removed very beautifully.

【0018】一方正リン酸2容量部、水2容量部を電解
液として上記と同等の仕上がり状態とするために概ね2
倍の時間がかかり、同じ60秒の処理時間では酸化物
(スケール)の除去ムラが明瞭に観察でき不十分な研磨
状態となった。
On the other hand, approximately 2 parts by volume of orthophosphoric acid and 2 parts by volume of water are used as electrolytes to obtain the same finished state as described above.
It took twice as long, and in the same processing time of 60 seconds, unevenness in removal of oxide (scale) was clearly observed, resulting in an insufficiently polished state.

【0019】[0019]

【発明の効果】以上のように本発明によれば、従来公知
の陽極溶解処理方法に比較して短時間でかつ良好な仕上
がり状態の金属を得ることができ、また取扱や装置に特
別の配慮を必要としないピロリン酸のカリウム塩、アン
モニウム塩のいずれか、あるいは両方を含有する水溶
液、もしくはポリリン酸水溶液をを電解液としているの
で、浸漬法、ブラシ法を問わず金属表面の陽極溶解処理
方法として幅広く適用することができる。
As described above, according to the present invention, it is possible to obtain a metal in a better finished state in a shorter time and in a shorter time than in the conventionally known anodic dissolution treatment method, and special consideration is given to handling and equipment. Aqueous solution containing either potassium salt or ammonium salt of pyrophosphoric acid, or both, or polyphosphoric acid aqueous solution is used as electrolyte, so anodic dissolution method of metal surface regardless of dipping method or brush method As widely applicable.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 小幡 惠吾 姫路市白浜町甲402番地 マルイ鍍金工 業有限会社内 (58)調査した分野(Int.Cl.7,DB名) C25F 1/04,3/02 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Keigo Obata 402 Shirahama-cho, Himeji-shi Marui Plating Industry Co., Ltd. (58) Field surveyed (Int. Cl. 7 , DB name) C25F 1/04, 3/02

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 金属表面の陽極溶解処理方法において、
ピロリン酸のカリウム塩、アンモニウム塩のいずれか、
あるいは両方を含有する水溶液、もしくはポリリン酸水
溶液を電解液とし、被処理金属を陽極に接続して直流で
電解処理を行うか、もしくは被処理金属に直流電源の陽
極に接続して該直流に交流を重畳させた電流で電解処理
を行うことを特徴とする金属表面の陽極溶解処理方法。
1. A method for anodic dissolution treatment of a metal surface,
One of potassium salt and ammonium salt of pyrophosphoric acid,
Alternatively, an aqueous solution containing both or an aqueous solution of polyphosphoric acid is used as an electrolytic solution, and the metal to be treated is connected to the anode to perform electrolytic treatment with a direct current, or the metal to be treated is connected to the anode of a DC power supply and the direct current is applied to the direct current. Anodic dissolution treatment method for a metal surface, wherein an electrolytic treatment is carried out with a current superimposed.
【請求項2】 上記電解液としてのピロリン酸のカリウ
ム塩、アンモニウム塩のいずれか、あるいは両方を含有
する水溶液の濃度を10〜50重量%とし、かつ該水溶
液のpHが9.5以下とした請求項1に記載の金属表面
の陽極溶解処理方法。
2. The concentration of an aqueous solution containing either or both of a potassium salt and an ammonium salt of pyrophosphoric acid as the electrolytic solution is adjusted to 10 to 50% by weight, and the pH of the aqueous solution is adjusted to 9.5 or less. The method for anodic dissolution treatment of a metal surface according to claim 1.
【請求項3】 上記電解液としてのポリリン酸水溶液の
濃度が10重量%以上とした請求項1に記載の金属表面
の陽極溶解処理方法。
3. The method according to claim 1, wherein the concentration of the aqueous solution of polyphosphoric acid as the electrolytic solution is 10% by weight or more.
JP3076015A 1991-04-09 1991-04-09 Anodizing treatment method for metal surface Expired - Lifetime JP3038249B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3076015A JP3038249B2 (en) 1991-04-09 1991-04-09 Anodizing treatment method for metal surface

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3076015A JP3038249B2 (en) 1991-04-09 1991-04-09 Anodizing treatment method for metal surface

Publications (2)

Publication Number Publication Date
JPH04311598A JPH04311598A (en) 1992-11-04
JP3038249B2 true JP3038249B2 (en) 2000-05-08

Family

ID=13593000

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3076015A Expired - Lifetime JP3038249B2 (en) 1991-04-09 1991-04-09 Anodizing treatment method for metal surface

Country Status (1)

Country Link
JP (1) JP3038249B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014131533A (en) * 2013-01-04 2014-07-17 Kiribai Kagaku Kk Coupling implement

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012011026A2 (en) 2010-07-22 2012-01-26 Koninklijke Philips Electronics N.V. Prevention or reduction of scaling on a heater element of a water heater
WO2012011051A1 (en) 2010-07-22 2012-01-26 Koninklijke Philips Electronics N.V. Prevention or reduction of scaling on a heater element of a water heater
CN106498484A (en) * 2016-10-25 2017-03-15 河北工业大学 A kind of electrolytic polishing method of complex brass
JP6746121B1 (en) * 2019-02-28 2020-08-26 株式会社日本科学エンジニアリング Electropolishing liquid for welding scale removal of stainless steel

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014131533A (en) * 2013-01-04 2014-07-17 Kiribai Kagaku Kk Coupling implement

Also Published As

Publication number Publication date
JPH04311598A (en) 1992-11-04

Similar Documents

Publication Publication Date Title
EP0075784B1 (en) Process for direct gold plating of stainless steel
US4740280A (en) Electrolyte for electrochemically polishing metal surfaces
JP3038249B2 (en) Anodizing treatment method for metal surface
JP2007332416A (en) Electrolytic solution for use in electropolishing process for stainless steel
JP2007332416A5 (en)
US4563257A (en) Method of electrolytically polishing a workpiece comprised of a nickel-, cobalt-, or iron-based alloy
JP2017160484A (en) Agent for removing weldment burnt deposit for electrolytic polishing and electrolytic polishing method
JP2007231413A (en) Electrolytic solution to be used for electrolytic polishing method for stainless steel
PL319470A1 (en) Method of treating outer surfaces of continuous casting mould components made of copper or its alloys, including nickel plating stage and stage of removing the nickel coating from that surface
US7094327B2 (en) Compositions for the treatment of magnesium alloys
JP2003193258A (en) Surface finishing method after descaling for stainless steel
JPS61207600A (en) Electrolytic descaling agent and descaling method for stainless steel
JPS6324098A (en) Method for removing scale formed by welding of alloy steel
JP2007277682A (en) Electrolytic solution used for electrolytic polishing method on stainless steel
JP3764774B2 (en) Method for pretreatment of magnesium or its alloy surface
JPH0127160B2 (en)
JPH02270999A (en) Method for removing weld burn of stainless steel
JP4500596B2 (en) Neutral electropolishing liquid composition for descaling of stainless steel surface and method for treating stainless steel surface
GB2205584A (en) Electrolytic treatment
JP3370015B2 (en) Finishing method for metal processed products
TWI527938B (en) Rapidly electrolytic rust removal method
WO1997039167A1 (en) Descaling of metal surfaces
JPS63100195A (en) Treating solution for anodically oxidizing magnesium or its alloy
US2357554A (en) Anodic treatment of ferrous metals
JP2011117031A (en) Method for treating metal surface