JPH04311598A - Anodic dissolving processing method for metal surface - Google Patents

Anodic dissolving processing method for metal surface

Info

Publication number
JPH04311598A
JPH04311598A JP7601591A JP7601591A JPH04311598A JP H04311598 A JPH04311598 A JP H04311598A JP 7601591 A JP7601591 A JP 7601591A JP 7601591 A JP7601591 A JP 7601591A JP H04311598 A JPH04311598 A JP H04311598A
Authority
JP
Japan
Prior art keywords
acid
aqueous solution
treatment
metal
treated
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.)
Granted
Application number
JP7601591A
Other languages
Japanese (ja)
Other versions
JP3038249B2 (en
Inventor
Yoshiaki Ida
義明 井田
Fumiyuki Tsudaka
文幸 津高
Hidetaka Ueda
上田 英貴
Keigo Obata
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 MEKKI KOGYO KK
Original Assignee
MARUI MEKKI KOGYO KK
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Filing date
Publication date
Application filed by MARUI MEKKI KOGYO KK filed Critical MARUI MEKKI KOGYO KK
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

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Abstract

PURPOSE:To offer an anodic dissolving processing method of a metal surface which makes a beautiful finishing with easy working and reduces processing time. CONSTITUTION:A electrolytic process is executed with a solution containing potassium salt and/on ammonium salt of pyrophosphoric acid or polyphosphoric acid aq. solution as an electrolytic solution by connecting a metal to be treated to an anodic electrode with direct current or by connecting the metal to be treated to the anodic electrode of direct power source with current which allows alternate current to superimpose the direct current.

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 the surface of metals such as stainless steel or copper alloys such as copper, brass, and 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。
[Prior Art] For example, alloy steel such as stainless steel that has been locally heated by welding, fusing, etc., copper and its alloys that have been heated during brazing, etc., or left in air for a long time. Oxide (scale) is generated on the surface,
The surface may lose its luster, impairing its appearance, or corrosion may occur at the locations where the oxide is generated. One method for removing oxides generated on the surface of such metals is anodic dissolution treatment.

【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。
[0003] Furthermore, the above-mentioned anodic dissolution treatment is sometimes applied in place of mechanical polishing, pickling, etc. for polishing and deburring metal surfaces, and even for etching treatment for producing name plates and nameplates. This anode dissolution treatment includes two methods: the immersion method, in which the metal to be treated connected to the anode is immersed in an electrolytic solution filled in a tank together with the electrode piece connected to the cathode; There is a brush method in which the surface of the metal to be treated is wiped while being energized with a treatment brush connected to a cathode covered with a water retentive 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 above immersion method is an aqueous solution of one or more strong acids selected from sulfuric acid, hydrochloric acid, nitric acid, hydrofluoric acid, phosphoric acid, etc., while the brush method uses the above immersion method. For example, in the descaling method for alloy steel described in Japanese Patent Publication No. 1-27160, the safer and more hygienic sodium salt of phosphoric acid is used as the electrolyte. , a single aqueous solution of potassium salt, ammonium salt, or sulfuric acid,
Adopting a mixed aqueous solution of sodium, potassium, and ammonium salts of nitric acid and hydrofluoric acid and a mixed aqueous solution of glycerin, there is no need for special consideration or equipment in handling or equipment as used in the above-mentioned immersion method. 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。
However, in such an anodic dissolution treatment method, the components of the electrolytic solution are important factors in determining the finished state of the treated surface of the metal to be treated and the slowness of the treatment speed. Particularly in the brush method, it is required that there is little unevenness in the finish near the periphery of the treated area. However, in the invention described in Japanese Patent Publication No. 1-27160, the processing speed is inferior to the method of processing using a strong acid as an electrolyte in the immersion method, and uneven finish may occur near the periphery of the treated area. It has been pointed out. These drawbacks are thought to be due to the use of orthophosphoric acid, which is less reactive than a strong acid alone aqueous solution such as sulfuric acid, hydrochloric acid, nitric acid, hydrofluoric acid, or phosphoric acid, as the electrolyte in the above-mentioned 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 dissolution treatment method for metal surfaces that is easy to handle, provides a beautiful finish, and shortens treatment time. The purpose is to

【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。
[Means for Solving the Problems] In order to achieve the above object, the present invention employs the following means. That is, in the anodic dissolution treatment method for metal surfaces, an aqueous solution containing either potassium salt of pyrophosphoric acid, ammonium salt, or both, or polyphosphoric acid aqueous solution is used as an electrolyte, and the metal to be treated is connected to the anode and subjected to direct current. The structure is such that electrolytic treatment is performed, or the metal to be treated is connected to the anode of a DC power source and electrolytic treatment is performed using a current in which alternating current is superimposed on the direct current.

【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 configuration is a general term for condensed phosphoric acids that are more reactive than orthophosphoric acid, and includes chain pyrophosphoric acid, triphosphoric acid, tetraphosphoric acid, and cyclic condensed phosphoric acid. Refers to a substance that includes certain trimetaphosphoric acid, tetrametaphosphoric acid, etc. By using such condensed phosphoric acid as a component of the electrolytic solution, the reactivity during electrolytic treatment is improved, resulting in beautiful and short treatment time. Processing can be done with .

【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。
[0009] The concentration of the aqueous solution containing either potassium salt or ammonium salt of pyrophosphoric acid, or both, contained in the aqueous solution as the electrolytic solution is 10 to 50% by weight.
If it is less than 10% by weight, anodic dissolution cannot be carried out within the desired treatment time, and if it exceeds 50% by weight, the solubility of the potassium salt and ammonium salt of pyrophosphoric acid will reach a saturated state, so electrolysis will not be possible. Unable to withstand use as a liquid. Furthermore, when a polyphosphoric acid aqueous solution is used as the electrolytic solution, it is desirable that its concentration be 10% by weight or more; if the concentration is less than 10% by weight, there is a risk that anodic dissolution may not be possible within the desired processing time. Undesirable.

【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。
Furthermore, when an aqueous solution containing either the potassium salt, the ammonium salt, or both of the above-mentioned pyrophosphoric acid is used as an electrolytic solution, it is desirable that the pH is 9.5 or less; If it exceeds this amount, the above-mentioned potassium salt and ammonium salt of pyrophosphoric acid may precipitate as crystals in the electrolytic solution, which is not preferable. In particular, a single solution of potassium salt of pyrophosphoric acid has a pH of 10 due to hydrolysis.
In addition to the fact that the above-mentioned tendency is remarkable because of the strong alkalinity of the before and after, in the brush method, for example, phosphoric acid ( It is desirable to lower the pH by adding a pH adjuster such as (not necessarily 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。
Note that the present invention does not preclude the addition of various substances for improving the finished state of the area treated by the anodic dissolution treatment. When performing anodic dissolution treatment using such an electrolyte, only direct current may be applied, but especially when performing scale removal treatment on stainless steel, it is necessary to keep the stainless steel in a high potential state for a long period of time. It is known that this causes the surface to passivate and takes a long time to process. Therefore, an alternating current with a maximum voltage slightly higher than the direct current is superimposed on the direct current to temporarily create a negative potential and the anode is dissolved. Accelerating the processing can also be done.

【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。
[Example] Hereinafter, an example to which the present invention is applied will be described and its effects will be verified. =Example 1= A brass sample with a brazed portion connected to the anode is immersed in an electrolytic solution in which phosphoric acid is added to an aqueous solution consisting of 100 g/l of potassium pyrophosphate and the pH is adjusted to 9.0. Then, anodic dissolution treatment was performed using direct current at a current density of 6 A/dm2. A brass sample with an extremely beautiful surface was obtained in a processing 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, as a control group, sodium sulfate 1
When anodic dissolution treatment was performed under the same treatment conditions as above using an aqueous solution of 0.00 g/l as the electrolyte, clear roughness of the substrate was observed. =Example 2= Phosphoric acid was added to an aqueous solution consisting of 350 g/l of potassium pyrophosphate, and a SUS304 stainless steel having a welded part connected to the anode was immersed in an electrolytic solution whose pH was adjusted to 8.0. Anodic dissolution treatment was performed using direct current at a current density of /dm2. The welding burn was removed very beautifully in a processing time of about 60 seconds.

【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, as a control group, sodium sulfate 2
When anodic dissolution treatment was performed under the same treatment conditions as above using an aqueous solution of 0.00 g/l as the electrolyte, it took a long time to remove the scale, and clear roughness of the substrate was observed. =Example 3=Aqueous ammonia was added to an aqueous solution consisting of 340 g/l of pyrophosphoric acid, and an ammonium pyrophosphate solution whose pH was adjusted to 3.5 was used as an electrolyte to impregnate the felt covering the electrode surface. Thereafter, the electrode was connected to the cathode, and a copper plate, which had turned brown due to natural standing, was connected to the anode, and anodic dissolution treatment was performed using a brush method in which a direct current of 6 V was applied. A copper plate with an extremely beautiful finish and restored luster was obtained in a processing time of about 60 seconds.

【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 in the electrolytic solution whose pH was adjusted to 4.5 using emery paper connected to the anode. A brass piece was immersed and subjected to an anodic melting treatment with direct current at a current density of 10 A/dm2. A brass piece that had regained its beautiful luster was obtained in about 30 seconds of processing time.

【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S
US304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
30V、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 consisting of 400 g/l of potassium pyrophosphate and the pH was adjusted to 7.5.The aqueous solution was used as an electrolyte and was impregnated into felt covering the electrode surface. After this, while connecting the electrode to the cathode, the S
US304 stainless steel was connected to the anode, a DC current with a voltage of 25 V was applied, and an AC current with a maximum voltage of 30 V and a frequency of 60 Hz was superimposed on the DC current to perform an anode melting process using the brush method. ,
The welding burn was removed very beautifully in 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SUS3
04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 group, ammonium sulfate 20
When the same treatment as above was carried out using a 0 g/l aqueous solution as the electrolyte, a strong pungent odor from ammonia was generated during the treatment process, and not only did it take a long time to remove the scale, but clear roughness of the substrate was observed. It 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. After this, while connecting the electrode to the cathode, the SUS3
When 04 stainless steel was connected to the anode and anodic dissolution treatment was carried out using a brush method in which a direct current of 25 V was applied for electrolytic treatment, welding burns were removed very beautifully in a treatment time of about 60 seconds.

【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 were used as an electrolyte to obtain the same finished state as above.
It takes twice as long, and with the same 60 second processing time, the oxide (
Uneven removal of scale) was clearly observed, resulting in insufficient polishing.

【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 metal in a better finished state in a shorter time than with conventionally known anodic melting treatment methods, and special consideration is given to handling and equipment. Since the electrolyte is an aqueous solution containing potassium salt, ammonium salt, or both of pyrophosphoric acid, or an aqueous polyphosphoric acid solution, it is suitable for anodic dissolution treatment of metal surfaces regardless of the immersion method or brush method. It can be widely applied as

Claims (3)

【特許請求の範囲】[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
Claim 1: In a method for anodic dissolution treatment of a metal surface, an aqueous solution containing either a potassium salt of pyrophosphoric acid, an ammonium salt, or both, or an aqueous polyphosphoric acid solution is used as an electrolyte, and the metal to be treated is connected to an anode. A method for anodic dissolution treatment of a metal surface, characterized in that the metal to be treated is electrolytically treated with a direct current, or the metal to be treated is connected to the anode of a direct current power source and the electrolytic treatment is performed with a current obtained by superimposing alternating current on the direct current.
【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。
[Claim 2] The concentration of the aqueous solution containing either a potassium salt or an ammonium salt of pyrophosphoric acid, or both, as the electrolytic solution is 10 to 50% by weight, and the pH of the aqueous solution is 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 anodic dissolution treatment method for a metal surface according to claim 1, wherein the concentration of the polyphosphoric acid aqueous solution 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 true JPH04311598A (en) 1992-11-04
JP3038249B2 JP3038249B2 (en) 2000-05-08

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9347684B2 (en) 2010-07-22 2016-05-24 Koninklijke Philips 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
US9986600B2 (en) 2010-07-22 2018-05-29 Koninklijke Philips N.V Prevention or reduction of scaling on a heater element of a water heater
JP2020139196A (en) * 2019-02-28 2020-09-03 株式会社日本科学エンジニアリング Welding scale removing electropolishing liquid for stainless steel

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6086730B2 (en) * 2013-01-04 2017-03-01 桐灰化学株式会社 Connector

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9347684B2 (en) 2010-07-22 2016-05-24 Koninklijke Philips N.V. Prevention or reduction of scaling on a heater element of a water heater
US9986600B2 (en) 2010-07-22 2018-05-29 Koninklijke Philips 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
JP2020139196A (en) * 2019-02-28 2020-09-03 株式会社日本科学エンジニアリング Welding scale removing electropolishing liquid for stainless steel

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