JPH01225800A - Method for removing oxide film in metallic material - Google Patents

Method for removing oxide film in metallic material

Info

Publication number
JPH01225800A
JPH01225800A JP5053888A JP5053888A JPH01225800A JP H01225800 A JPH01225800 A JP H01225800A JP 5053888 A JP5053888 A JP 5053888A JP 5053888 A JP5053888 A JP 5053888A JP H01225800 A JPH01225800 A JP H01225800A
Authority
JP
Japan
Prior art keywords
oxide film
liquid
felt material
pipe
absorbing member
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
JP5053888A
Other languages
Japanese (ja)
Inventor
Shigeru Hotsuta
堀田 ▲しげ▼
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.)
GIRUFUII KK
Original Assignee
GIRUFUII KK
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 GIRUFUII KK filed Critical GIRUFUII KK
Priority to JP5053888A priority Critical patent/JPH01225800A/en
Publication of JPH01225800A publication Critical patent/JPH01225800A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To rapidly remove an oxide film from the surface of a metallic material by rubbing the surface of the oxide film of a metallic member with a liq. absorptive member impregnated with an acidic processing soln. while carrying out electrolysis with a locally high current density. CONSTITUTION:A cylindrical body 4 (e.g., a pipe 10) having an oxide film 12 is horizontally fixed to a rotating mechanism 6, and the liq. absorptive member such as a felt material 16 is supported by a concentric receiving plate 14 set under the cylindrical body 4. When the device 2 is operated, a high current density is locally generated below the right end of the receiving plate 14 and the upper surface at the right end of the felt material 16. Meanwhile, when a dil. acid processing soln. is injected 24, the soln. flows over the pipe surface and is absorbed by the felt material 16. When the pipe 10 is rotated, the film 12 on the pipe surface is rubbed by the felt material 16, and the film 12 is successively separated and removed along the circumference. In this case, the spent dil. acid processing soln. is sent to a tank 22 by a pump 20 from the receiving plate 14, and circulated. Consequently, only a small amt. of the fresh soln. is replenished, and waste liq. is hardly generated.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、金属材料を空気中で熱処理した際::生じる
比較的厚い酸化物皮膜を迅速に除去する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for rapidly removing a relatively thick oxide film formed when a metal material is heat treated in air.

(従来の技術) 金属材料例えばステンレス鋼材料を空気中で溶接すると
溶接線に沿って帯状に酸化物皮膜を生じ、このデスケー
リングには主として硫酸又は塩酸を用いている。金属材
料を硫酸又は塩酸溶液に浸漬する場合、硫酸では約20
%までビックリング速度が増加し、同濃度で同温度では
塩酸の方が硫酸よりも1.5〜2.0倍デスケーリング
が早いけれども、いずれもミストが発生するために排気
洗浄装置を設置する必要がある。この改良方法には塩酸
溶液を含むゼリー状物が存在し、これを金属材料の酸化
物皮膜の上に塗り、約30分後に水で洗い流している。
(Prior Art) When metal materials such as stainless steel materials are welded in air, a band-shaped oxide film is formed along the weld line, and sulfuric acid or hydrochloric acid is mainly used for descaling. When immersing metal materials in sulfuric acid or hydrochloric acid solution, approximately 20
%, and descaling is 1.5 to 2.0 times faster with hydrochloric acid than with sulfuric acid at the same concentration and temperature, but both generate mist, so an exhaust cleaning device must be installed. There is a need. This improved method includes a jelly containing a hydrochloric acid solution, which is applied onto the oxide film of the metal material and washed off with water after about 30 minutes.

また、銀粉入りペンキを帯状の酸化物皮膜に沿って塗布
し、該酸化物皮膜を隠遮する方法がある。酸による方法
としては、硫酸の5〜20%溶液中で陰極電解、陽極電
解、PR電解を行う方法もある。
There is also a method of applying paint containing silver powder along a band-shaped oxide film to conceal and shield the oxide film. As a method using an acid, there is also a method of performing cathodic electrolysis, anodic electrolysis, and PR electrolysis in a 5 to 20% solution of sulfuric acid.

(発明が解決しようとする課題) 塩酸溶液を含むゼリー状物を用いると、洗い流した水に
は臭気があって池の物質を腐食するために、排水の処理
に関して公害問題が発生する。このゼリー状物は、加温
すれば除去効果が増加するけれども、酸化物皮膜上に塗
ったままで長時間放置することを要し、作業効率が悪い
という問題が残っている。また、銀粉入りペンキの塗布
は、塗布コストが高いうえに使用中にペンキが剥がれや
すい。電解による方法は、強固な酸化物皮膜でも迅速に
除去できるけれども、電解設備が必要でコスト高になる
うえに、凹部の酸化物皮膜が凸部に比べて溶解が遅れ、
しかも排水処理の問題は依然として残存している。
(Problem to be Solved by the Invention) When a jelly-like material containing a hydrochloric acid solution is used, a pollution problem occurs in the treatment of wastewater because the water used for washing has an odor and corrodes the pond materials. Although the removal effect of this jelly-like material increases if it is heated, there remains the problem that it is necessary to leave it on the oxide film for a long time, resulting in poor working efficiency. Furthermore, applying paint containing silver powder is expensive, and the paint tends to peel off during use. Although the electrolytic method can quickly remove even strong oxide films, it requires electrolytic equipment and is expensive, and the oxide film on concave areas dissolves more slowly than on convex areas.
Moreover, the problem of wastewater treatment still remains.

本発明は、金属材料における酸化物皮膜の除去技術に関
する前記の問題点を改善するために提案されたものであ
り、強固な酸化物皮膜であっても迅速且つ容易に除去し
、しかも安価な電解装置を用いて廃液処理の問題が殆ど
発生しない酸化物皮膜の除去方法を提供することを目的
としている。
The present invention was proposed in order to improve the above-mentioned problems related to the technology for removing oxide films from metal materials, and it can quickly and easily remove even strong oxide films using an inexpensive electrolytic method. The object of the present invention is to provide a method for removing an oxide film using a device that hardly causes problems in waste liquid treatment.

(課題を解決するための手段) 上記目的を達成するために、本発明に係る酸化物皮膜の
除去方法では、吸液性部材を一方の電極体に取り付け、
且つ他方の電極体を金属材料に接触させる。この吸液性
材料は、綿を布地で包んたタンボ、フェルト、スポンジ
などであって、酸処理液を十分に吸収・保持し且つ耐摩
耗性を有すると好ましく、一方、両電極体は焼結炭素な
どの不溶解性電極材料であると好ましい。両電極体間に
外部電源を用いて所定の電位を加えるために、吸液性部
材をアノード又はカソード電極体に取りはけ、且つその
反対の電極体を金属材料表面に接触させるけれども、P
R法による電解も可能である。
(Means for Solving the Problems) In order to achieve the above object, in the method for removing an oxide film according to the present invention, a liquid absorbing member is attached to one electrode body,
In addition, the other electrode body is brought into contact with a metal material. This liquid-absorbing material is preferably a cotton pad wrapped in cloth, felt, sponge, etc., which can sufficiently absorb and retain the acid treatment solution and has wear resistance.On the other hand, both electrode bodies are made of sintered material. Preferably, it is an insoluble electrode material such as carbon. In order to apply a predetermined potential between both electrode bodies using an external power source, a liquid absorbing member is attached to the anode or cathode electrode body, and the opposite electrode body is brought into contact with the surface of the metal material.
Electrolysis by the R method is also possible.

両電極体を金属材料上で近接させて局所的に高い電流密
度を発生させ、アノード電極S:おいてSO2などの気
体を多く発生させないように電圧を低く抑える。吸液性
部材には、主成分が硫酸又は塩酸などの酸処理液を含浸
し、通常は後処理の容易な希酸処理液を含浸して酸化物
皮膜と接触させ、所望に応じて希酸処理液にインヒビタ
ーなどを添加してもよい。次に吸液性部材又は金属材料
を酸化物皮膜に沿って相対的に移動し、この移動には手
動(第3図参照)又は適宜の駆動装置(第1図又は第5
図参照)を用いる。処理可能な金属材料は、ステンレス
鋼などの各種の鉄鋼、アルミニウム。
Both electrode bodies are brought close to each other on a metal material to locally generate a high current density, and the voltage is kept low so as not to generate a large amount of gas such as SO2 at the anode electrode S. The liquid-absorbing member is impregnated with an acid treatment liquid whose main component is sulfuric acid or hydrochloric acid, and is usually impregnated with a dilute acid treatment liquid that can be easily post-treated and brought into contact with the oxide film. An inhibitor or the like may be added to the treatment solution. Next, the liquid-absorbing member or the metal material is moved relatively along the oxide film, and this movement can be done manually (see Figure 3) or by an appropriate drive device (see Figure 1 or 5).
(see figure). Metal materials that can be processed include various types of steel such as stainless steel, and aluminum.

亜鉛とその合金などである。ステンレス鋼材料では、溶
接などで生じた表面の酸化物皮膜を吸水性部材で摩擦し
て分離した後に、活性化したその分離部分にニッケルメ
ッキを行う場合もある。
These include zinc and its alloys. In the case of stainless steel materials, after the oxide film on the surface produced by welding or the like is separated by friction with a water-absorbing member, the activated separated part is sometimes plated with nickel.

(作用) 本発明方法では、局所的に高い電流密度で電解しながら
、酸処理液を含浸した吸液性部材で金属材料の酸化物皮
膜表面を摩擦することにより、金属材料表面から酸化物
皮膜を迅速に分離して除去する。処理する金属材料に関
して、カノード電解では金属材料の腐食は少なく、寸法
精度を維持でき、しかも活性化されるためにメツキの密
着にもよい反面、水素ガスが発生するので水素脆性の起
こしやすい高炭素鋼やばね鋼には好ましくない。
(Function) In the method of the present invention, the oxide film is removed from the surface of the metal material by rubbing the surface of the oxide film on the metal material with a liquid-absorbing member impregnated with an acid treatment liquid while locally electrolyzing at a high current density. quickly separate and remove. Regarding the metal materials to be treated, cathode electrolysis causes less corrosion of metal materials, maintains dimensional accuracy, and is good for plating adhesion because it is activated. Not suitable for steel and spring steel.

一方、アノード電解では、酸化物皮膜を酸素ガスで物理
的に剥離し、金属材料表面の不動悪化が生じて腐食を防
止し、水素脆性の発生を緩和できる反面、化学的に活性
なアルミニウム、亜鉛とその合金には通さない。
On the other hand, in anodic electrolysis, the oxide film is physically removed using oxygen gas, making the surface of the metal material immobile, preventing corrosion, and mitigating the occurrence of hydrogen embrittlement. and its alloys.

(実施例) 次に本発明方法の実施例を図面を参照しながら説明する
゛。
(Example) Next, an example of the method of the present invention will be described with reference to the drawings.

実施例1 第1図に示す洗浄装置2において、除去すべき酸化物皮
膜を有する円筒体4は回転機構6のチャック8に水平に
取り付け、該回転機構は旋盤の主軸台などを利用すれば
よい。円筒体4は、例えば第2図に示す溶接パイプ10
であり、該パイプ表面に溶接線に沿って環状の酸化物皮
膜12が生じている。円筒体4即ちバイブ10の下方に
は、該バイブと同心の円弧状側面の受板14を設置し、
該受板で吸液性部材例えば帯状のフェルト材16を支持
する。受は板14は逆U字形の横断面であり、その内表
面に帯状のフェルト材16を沿わすことにより、該フェ
ルト材も側面円弧状:こ変形してパイプ10の表面に接
触する。受板14の下端部には送液管18を連通させ、
循環ポンプ20を経て落差タンク22まで延設する。タ
ンク22は、送液管23を介してノズル24に希酸処理
液を送っている。適宜の外部直流電源26から、ノズル
24の先端部と受板14の右端部に配線することにより
、受板右端部が一方の電極体及びパイプ10の表面と接
触するノズル先端部が他方の電極体に相当する。第1図
では、ノズル先端部がアノード電極体であるが、この先
端部はカソード電極体にしてもよく、又はPR雷電流用
いてもよい。
Embodiment 1 In the cleaning apparatus 2 shown in FIG. 1, the cylindrical body 4 having the oxide film to be removed is horizontally attached to the chuck 8 of the rotating mechanism 6, and the rotating mechanism may be a headstock of a lathe or the like. . The cylindrical body 4 is, for example, a welded pipe 10 shown in FIG.
A ring-shaped oxide film 12 is formed on the pipe surface along the weld line. Below the cylindrical body 4, that is, the vibrator 10, a receiving plate 14 with an arcuate side surface concentric with the vibrator is installed,
A liquid-absorbing member such as a strip-shaped felt material 16 is supported by the receiving plate. The receiving plate 14 has an inverted U-shaped cross section, and by placing a strip of felt material 16 along its inner surface, the felt material also deforms into an arcuate side surface and comes into contact with the surface of the pipe 10. A liquid sending pipe 18 is communicated with the lower end of the receiving plate 14,
It extends to the head tank 22 via the circulation pump 20. The tank 22 sends the dilute acid treatment liquid to the nozzle 24 via the liquid sending pipe 23. By wiring an appropriate external DC power supply 26 to the tip of the nozzle 24 and the right end of the receiving plate 14, the right end of the receiving plate contacts one electrode body and the surface of the pipe 10 contacts the other electrode. corresponds to the body. In FIG. 1, the nozzle tip is an anode electrode body, but this tip may be a cathode electrode body, or a PR lightning current may be used.

この装置2を作動すれば、フェルト材14の右端部にお
いて受板右端部とパイプ表面との間に局所的の高い電流
密度が発生する。一方、ノズル24から希酸処理液を噴
射すると、この処理液はパイプ表面を流れてフェルト材
16で吸収され、該フェルト材に常に希酸処理液を含浸
させることになる。フェルト材16はパイプ10の表面
と接触しているから、該パイプをチャック8で回転する
と、フェルト材16でパイプ表面の酸化物皮膜12を摩
擦し、酸化物皮膜12を円周に沿って順次分離していく
。使用済みの希酸処理液は、ポンプ20によって受板1
4からタンク22に送って循環させ、少量の新液を補給
するたけであるから廃液は殆ど発生しない。
When this device 2 is operated, a localized high current density is generated at the right end of the felt material 14 between the right end of the receiving plate and the pipe surface. On the other hand, when the dilute acid treatment liquid is injected from the nozzle 24, this treatment liquid flows on the pipe surface and is absorbed by the felt material 16, so that the felt material is constantly impregnated with the dilute acid treatment liquid. Since the felt material 16 is in contact with the surface of the pipe 10, when the pipe is rotated by the chuck 8, the felt material 16 rubs the oxide film 12 on the pipe surface, and the oxide film 12 is sequentially removed along the circumference. Separate. The used dilute acid treatment liquid is transferred to the receiving plate 1 by the pump 20.
4 to the tank 22 for circulation and replenishing a small amount of new liquid, almost no waste liquid is generated.

この洗浄装置において、受板14の代わりに、フェルト
材を巻き付けたローラ(第5図参照)を使用することも
可能である。また、液循環回路の代わりに、必要量の希
酸処理液だけを受板14の右端部に強制的に送るように
してもよい。
In this cleaning device, it is also possible to use a roller wrapped with felt material (see FIG. 5) instead of the receiving plate 14. Further, instead of the liquid circulation circuit, only the necessary amount of dilute acid treatment liquid may be forcibly sent to the right end of the receiving plate 14.

実施例2 第3図に示す洗浄機器30において、中空の機器本体3
2は細長く、その上方部34は水平に屈曲している。タ
ンポ36である吸液性部材を一方の棒状電極体38の先
端に取り付け、該電極体と近接させて他方の棒状電極体
40を上方に配置し、両電極体を機器上方部34の先端
面に水平に設置する。電極体40の先端は通常尖り、タ
ンボ36の前面よりもやや前方に位置させ、電極体40
は機器本体32内のばね42によって前方へ付勢する。
Example 2 In the cleaning equipment 30 shown in FIG.
2 is elongated and its upper part 34 is bent horizontally. A liquid-absorbing member, which is a pad 36, is attached to the tip of one rod-shaped electrode body 38, and the other rod-shaped electrode body 40 is placed above the rod-shaped electrode body in close proximity to the electrode body, and both electrode bodies are attached to the tip surface of the upper part 34 of the device. Install it horizontally. The tip of the electrode body 40 is usually pointed, and is positioned slightly forward of the front surface of the button 36.
is biased forward by a spring 42 within the device body 32.

両電極体38.40は、手動操作のスイッチ44を経て
外部電源(図示しない)に配線し、該外部電源は例えば
交流電源に接続する定電圧直流電源である。
Both electrode bodies 38, 40 are wired via a manually operated switch 44 to an external power source (not shown), which is, for example, a constant voltage DC power source connected to an AC power source.

この機器3oは、機器本体32を手で握って使用し、タ
ンボ36を希酸処理液に漬ける際には操作スイッチ44
を離して電流を流さない。第4図に例示するように、タ
ンボ36に希酸処理液を含浸した復に、金属材料の酸化
物皮膜46の上にタンポ36及び電極体40を当てて通
電すると、タンポ36において電極体38の先端と金属
材料表面との間に局所的の高い電流密度が発生する。タ
ンポ36及び電極体40を金属材料表面と接触させなが
ら、機器30を任意の形状の酸化物皮膜46に沿って動
かすと、該タンボで酸化物皮膜46を摩擦して順次分離
する。消費した希酸処理液は、その都度タンボ36を希
酸処理液に漬けるだけであるから少量で済み、本格的な
処理設備を必要とする。はどの廃液は発生しない。
This device 3o is used by holding the device main body 32 by hand, and when immersing the button 36 in the dilute acid treatment liquid, use the operation switch 4.
Do not apply current by separating the As illustrated in FIG. 4, when the tampon 36 is impregnated with a dilute acid treatment liquid and then the tampon 36 and the electrode body 40 are applied to the oxide film 46 of the metal material and energized, the electrode body 38 at the tampon 36 A localized high current density is generated between the tip of the metal material and the surface of the metal material. When the device 30 is moved along the arbitrarily shaped oxide film 46 while the pad 36 and the electrode body 40 are in contact with the surface of the metal material, the oxide film 46 is rubbed by the pad and separated one by one. Since the tank 36 is simply immersed in the dilute acid treatment liquid each time, only a small amount of the consumed dilute acid treatment liquid is needed, and full-scale treatment equipment is not required. No waste liquid is generated.

第3図の洗浄機器30では、タンポ36を希酸処理液に
漬けて使用するけれども、希酸処理液を入れたタンクを
機器30に取り付け、該タンクから直接タンボ36まて
希酸処理液を送るようにしてもよい。また、定置型の外
部電源の代わりに、機器本体に所定電圧の乾電池や充電
器を収納したり、又は使用者の腰ベルトに小型電源を取
り付けるようにしてもよい。これらの変形で洗浄機器の
可搬性がいっそう良くなり、不便な個所の溶接で生じた
酸化物皮膜でも容易に除去可能になる。
In the cleaning device 30 shown in FIG. 3, the tampon 36 is immersed in a dilute acid treatment solution, but a tank containing the dilute acid treatment solution is attached to the device 30, and the tank 36 is directly poured from the tank. You may also send it. Furthermore, instead of a stationary external power source, a dry battery or charger of a predetermined voltage may be housed in the main body of the device, or a small power source may be attached to the user's waist belt. These modifications make the cleaning equipment even more portable and allow for easier removal of oxide films created by welding in inconvenient locations.

実施例3 第5図に示す洗浄装置50において、除去すべき直線状
の酸化物皮膜51を有する金属プレート52は、該皮膜
を下側に位置させてローラ54゜56によって水平に走
行させる。ローラ54,56間には、洗浄ローラ58を
配置し、その円周に吸液性部材であるフェルト材60を
巻き付ける。
Embodiment 3 In a cleaning device 50 shown in FIG. 5, a metal plate 52 having a linear oxide film 51 to be removed is moved horizontally by rollers 54 and 56 with the film positioned on the lower side. A cleaning roller 58 is disposed between the rollers 54 and 56, and a felt material 60, which is a liquid-absorbing member, is wrapped around the circumference of the cleaning roller 58.

環状のフェルト材60は、上端を金属プレート52の下
側と接触させ、且つその下端を液浴62に浸漬させる。
The annular felt material 60 has its upper end in contact with the lower side of the metal plate 52 and its lower end is immersed in the liquid bath 62 .

液浴62には希酸処理液を入れ、該液の補給は管64を
介してポンプ66で行う。画電極体68.70は、適宜
の外部電源72と配線したロータであり、プレート52
とフェルト材60の接触個所において該プレート上側と
ローラ58の内周壁に当接しながら回転する。
A dilute acid treatment solution is placed in the liquid bath 62, and the solution is replenished by a pump 66 via a pipe 64. The picture electrode body 68,70 is a rotor wired with an appropriate external power source 72, and the plate 52
The plate rotates while abutting the upper side of the plate and the inner circumferential wall of the roller 58 at the contact point between the felt material 60 and the felt material 60 .

この装置50を作動すれば、プレート52とフェルト材
60の接触個所において局所的の高い電流密度が発生す
る。一方、液浴62内の希酸処理液は、フェルト材60
の下端で吸収され、該フェルト材の回転によってその上
端まで達する。洗浄ローラ60の回転速度は、ローラ5
4,56の回転つまりプレート5・2の走行速度と異な
ることにより、フェルト材60でプレート下側の酸化物
皮膜51を摩擦し、プレート52の走行とともに酸化物
皮膜51を直線状に順次分離していく。希酸処理7αは
、プレート52に付着する分だけをポンプ66で補充す
ればよく、少量の新液補給だけであるから廃液は殆ど発
生しない。
When the device 50 is operated, a localized high current density is generated at the contact point between the plate 52 and the felt material 60. On the other hand, the dilute acid treatment liquid in the liquid bath 62 is applied to the felt material 60.
It is absorbed at the lower end of the felt material and reaches its upper end by rotation of the felt material. The rotation speed of the cleaning roller 60 is the same as that of the roller 5.
Due to the rotation of the plates 5 and 56, which is different from the traveling speed of the plates 5 and 2, the felt material 60 rubs the oxide film 51 on the lower side of the plate, and as the plate 52 travels, the oxide film 51 is linearly separated one by one. To go. In the dilute acid treatment 7α, only the amount that adheres to the plate 52 needs to be replenished by the pump 66, and since only a small amount of new liquid is replenished, almost no waste liquid is generated.

この洗浄装置において、希酸処理液をローラ58の内部
中心に送り、そこから放射状に円周部分のフェルト材6
0まて浸出させてもよい。また、ローラ54,56を使
用せずに、プレート52を手でフェルト材60に圧着す
るならば、部分的な酸化物皮膜を除去することが可能で
ある。
In this cleaning device, the dilute acid treatment liquid is sent to the inner center of the roller 58, and from there it is radially distributed around the felt material 6 at the circumferential portion.
It may also be leached. Moreover, if the plate 52 is manually pressed onto the felt material 60 without using the rollers 54 and 56, it is possible to partially remove the oxide film.

(発明の効果) 本発明方法では、局所的に高い電流密度で電解しなから
吸液性部材て金属材料の酸化物皮膜表面を摩擦すること
により、金属材料から酸化物皮膜を迅速且つ容易に除去
し、従来の方法に比べて作業効率が優れ且つ作業環境の
悪化も殆ど起こらない。本発明方法は、通常の電解方法
に比べて電解設備が単純で設備コストが安く、吸液性部
材による摩擦を行うために、凹部の酸化物皮膜が凸部に
比べて溶解が遅れるようなことが殆ど発生しない。
(Effects of the Invention) In the method of the present invention, the oxide film can be quickly and easily removed from the metal material by locally electrolyzing at a high current density and then rubbing the oxide film surface of the metal material with a liquid-absorbing member. The work efficiency is superior to that of conventional methods, and there is almost no deterioration of the work environment. The method of the present invention has simpler electrolytic equipment and lower equipment cost than normal electrolysis methods, and because the liquid-absorbing member performs friction, the oxide film on the recesses does not dissolve more slowly than on the protrusions. rarely occurs.

また、本発明方法は、一般に希酸処理液を少量使用する
だけであるから、電解浴を設置する電解方法よりも廃液
の生成が少なく、この希酸処理液は臭気が少なくて池の
物質を腐食せず、排水の処理$2関して公害問題が発生
する恐れも少ない。
In addition, since the method of the present invention generally uses only a small amount of dilute acid treatment solution, less waste fluid is produced than in the electrolytic method that uses an electrolytic bath. It does not corrode and there is little risk of pollution problems related to wastewater treatment.

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

第1図は本発明方法を実施するための装置を概略的に示
す全体説明図、第2図は環状の酸化物皮膜を有する溶接
パイプの一例を示す斜視図、第3図は本発明方法を実施
するための別の装置の側面図、第4図は第3図の使用状
態を示す要部側面図、第5図は本発明方法を実施するた
めの更に別の装置の側面図である。 2・・・洗浄装置、4・・・円筒体、6・・・回転機構
、8・・・チャック、10・・・溶接パイプ、12・・
・酸化物皮膜、 14・・・受板、 16・・・フェル
ト材、20・・・循環ポンプ、22・・・落差タンク、
24・・・ノズル、26・・・外部直流電源。 特許出願人 ギルフィー株式会社
Fig. 1 is an overall explanatory diagram schematically showing an apparatus for carrying out the method of the present invention, Fig. 2 is a perspective view showing an example of a welded pipe having an annular oxide film, and Fig. 3 is a diagram illustrating the method of the present invention. FIG. 4 is a side view of a main part showing the usage state of FIG. 3, and FIG. 5 is a side view of still another device for implementing the method of the present invention. 2...Cleaning device, 4...Cylindrical body, 6...Rotating mechanism, 8...Chuck, 10...Welded pipe, 12...
- Oxide film, 14... Reception plate, 16... Felt material, 20... Circulation pump, 22... Head tank,
24... Nozzle, 26... External DC power supply. Patent applicant Gilphy Co., Ltd.

Claims (1)

【特許請求の範囲】 1、金属材料を空気中で熱処理した際に生じる比較的厚
い酸化物皮膜を除去するために、吸液性部材を一方の電
極体に取り付け且つ他方の電極体を金属材料に接触させ
、両電極体間に外部電源を用いて所定の電位を加えて局
所的に高い電流密度を発生させるとともに、吸液性部材
に酸処理液を含浸して酸化物皮膜と接触させ、次に吸液
性部材又は金属材料を酸化物皮膜に沿って相対的に移動
して吸液性部材で酸化物皮膜の表面を摩擦することによ
り、金属材料の酸化物皮膜を順次分離していく酸化物皮
膜の除去方法。 2、ステンレス鋼材料表面の酸化物皮膜を、希酸処理液
を含浸した吸液性部材で摩擦して分離した後に、活性化
したその分離部分にニッケルメッキを行う請求項1記載
の方法。
[Claims] 1. In order to remove a relatively thick oxide film that occurs when a metal material is heat-treated in air, a liquid-absorbing member is attached to one electrode body, and the other electrode body is made of a metal material. and apply a predetermined potential between both electrode bodies using an external power source to generate a locally high current density, and impregnate the liquid-absorbing member with an acid treatment liquid and bring it into contact with the oxide film. Next, the liquid-absorbing member or metal material is moved relatively along the oxide film, and the liquid-absorbing member rubs the surface of the oxide film, thereby sequentially separating the oxide film of the metal material. How to remove oxide film. 2. The method according to claim 1, wherein the oxide film on the surface of the stainless steel material is separated by rubbing with a liquid-absorbing member impregnated with a dilute acid treatment solution, and then the activated separated part is plated with nickel.
JP5053888A 1988-03-02 1988-03-02 Method for removing oxide film in metallic material Pending JPH01225800A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5053888A JPH01225800A (en) 1988-03-02 1988-03-02 Method for removing oxide film in metallic material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5053888A JPH01225800A (en) 1988-03-02 1988-03-02 Method for removing oxide film in metallic material

Publications (1)

Publication Number Publication Date
JPH01225800A true JPH01225800A (en) 1989-09-08

Family

ID=12861784

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5053888A Pending JPH01225800A (en) 1988-03-02 1988-03-02 Method for removing oxide film in metallic material

Country Status (1)

Country Link
JP (1) JPH01225800A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITUB20154984A1 (en) * 2015-10-16 2017-04-16 Condoroil Stainless Srl ELECTROLYTIC PICKLING PROCESS FOR STAINLESS STEELS

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53102840A (en) * 1977-02-21 1978-09-07 Mitsubishi Heavy Ind Ltd Preliminarily treating method for diffusion welding of stainless steel, aluminum or aluminum alloy
JPS559080A (en) * 1978-06-29 1980-01-22 Merck & Co Inc Substituted dihydropyridine urea

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53102840A (en) * 1977-02-21 1978-09-07 Mitsubishi Heavy Ind Ltd Preliminarily treating method for diffusion welding of stainless steel, aluminum or aluminum alloy
JPS559080A (en) * 1978-06-29 1980-01-22 Merck & Co Inc Substituted dihydropyridine urea

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITUB20154984A1 (en) * 2015-10-16 2017-04-16 Condoroil Stainless Srl ELECTROLYTIC PICKLING PROCESS FOR STAINLESS STEELS

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