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JP5522482B2 - Surface treatment equipment - Google Patents
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JP5522482B2 - Surface treatment equipment - Google Patents

Surface treatment equipment Download PDF

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JP5522482B2
JP5522482B2 JP2011112575A JP2011112575A JP5522482B2 JP 5522482 B2 JP5522482 B2 JP 5522482B2 JP 2011112575 A JP2011112575 A JP 2011112575A JP 2011112575 A JP2011112575 A JP 2011112575A JP 5522482 B2 JP5522482 B2 JP 5522482B2
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electrode member
electrolyte
negative electrode
peripheral surface
positive electrode
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JP2012007234A (en
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大之 小林
和宏 龍本
誠喜 加藤
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Aisin Corp
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Aisin Seiki Co Ltd
Aisin Corp
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/02Electroplating of selected surface areas
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D11/00Electrolytic coating by surface reaction, i.e. forming conversion layers
    • C25D11/005Apparatus specially adapted for electrolytic conversion coating
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D17/00Constructional parts, or assemblies thereof, of cells for electrolytic coating
    • C25D17/10Electrodes, e.g. composition, counter electrode
    • C25D17/12Shape or form

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electroplating Methods And Accessories (AREA)

Description

本発明は表面処理装置に関する。   The present invention relates to a surface treatment apparatus.

従来の表面処理装置は、例えば、環状被処理領域としての周溝を外周面に有する金属製の被処理物に電気的に接続される陽電極部材と、前記外周面及び前記周溝に対して間隔を隔てて対向する内周面を備えた枠部材と、前記外周面のうち前記周溝を挟んだ両側夫々と前記内周面との隙間をシールすることにより、前記周溝に沿った電解液通路を形成可能な非導電性の弾性シール材と、前記電解液通路に設けてある陰電極部材と、前記電解液通路に沿って電解液を通流させる電解液通流手段とを備えている。
上記表面処理装置は、被処理物の外周面に有する環状被処理領域に沿った電解液通路を形成して、その電解液通路に沿って電解液を通流させながら、例えば陽極酸化処理などの表面処理を環状被処理領域に対して効率良く行うことができる。
従来の上記表面処理装置では、枠部材を導電性の材料で形成して、この枠部材で、被処理物の外周面及び環状被処理領域(周溝)に対して間隔を隔てて対向する環状の内周面を有する陰電極部材を構成してある(例えば、特許文献1参照)。
The conventional surface treatment apparatus is, for example, a positive electrode member that is electrically connected to a metal workpiece having a circumferential groove as an annular treatment region on the outer circumferential surface, and the outer circumferential surface and the circumferential groove. Electrolysis along the circumferential groove is performed by sealing a gap between the inner circumferential surface and a frame member having inner circumferential surfaces facing each other with a gap therebetween, and both sides of the outer circumferential surface sandwiching the circumferential groove. A non-conductive elastic sealing material capable of forming a liquid passage, a negative electrode member provided in the electrolyte passage, and an electrolyte flow means for flowing the electrolyte along the electrolyte passage. Yes.
The surface treatment apparatus forms an electrolyte passage along the annular treatment area on the outer peripheral surface of the object to be treated, and allows the electrolyte solution to flow along the electrolyte passage while, for example, anodizing. The surface treatment can be efficiently performed on the annular processing region.
In the conventional surface treatment apparatus, the frame member is formed of a conductive material, and the frame member is annularly opposed to the outer peripheral surface of the object to be processed and the annular treatment region (circumferential groove) with a space therebetween. The negative electrode member which has the inner peripheral surface of is comprised (for example, refer patent document 1).

特開2003−119593号公報(段落番号[0024])JP 2003-119593 A (paragraph number [0024])

上記表面処理装置は、表面処理時における陽電極部材と陰電極部材とに亘る通電により、電解液に溶解している陽イオン化し易い銅などの金属成分が陰電極部材の表面に析出して付着堆積し易い。
従来の表面処理装置は、環状の内周面を有する陰電極部材を設けてあるために、析出金属が陰電極部材の内周面に全周に亘って均一に付着堆積し易く、堆積した析出金属によって電解液通路の通路断面積が狭められると電解液の円滑な通流が妨げられる。
尚、枠部材が、被処理物の外周面及び環状被処理領域に対して間隔を隔てて対向する環状の内周面を有する陽電極部材を構成している場合は、電解液に溶解している陰イオン化し易い塩化物や硫化物などの非金属成分が陽電極部材の表面に析出して、同様の現象が生じる。
電解液の温度は、電極反応で発生する熱により環状被処理領域の表面近傍で高くなり、電解液の円滑な通流が妨げられると、電解液の温度が上昇し易い。
電解液の温度が上昇すると、例えばアルマイト被膜などの被膜を環状被処理領域に形成する表面処理において所謂ヤケが生じ易くなり、表面処理を高い電圧で能率良く繰り返し行うことができないおそれがある。
本発明は上記実情に鑑みてなされたものであって、表面処理を高い電圧で能率良く繰り返し行うことができる表面処理装置を提供することを目的とする。
In the above surface treatment apparatus, due to energization between the positive electrode member and the negative electrode member at the time of the surface treatment, metal components such as copper which is easily cationized dissolved in the electrolytic solution are deposited on the surface of the negative electrode member. Easy to deposit.
Since the conventional surface treatment apparatus is provided with a negative electrode member having an annular inner peripheral surface, the deposited metal tends to adhere and deposit uniformly on the inner peripheral surface of the negative electrode member over the entire circumference, and the deposited precipitation When the passage cross-sectional area of the electrolyte passage is narrowed by the metal, the smooth flow of the electrolyte is hindered.
In addition, when the frame member constitutes a positive electrode member having an annular inner peripheral surface that is opposed to the outer peripheral surface of the object to be processed and the annular processing region with a gap, the frame member is dissolved in the electrolytic solution. The same phenomenon occurs when non-metallic components such as chlorides and sulfides that are easily anionized are deposited on the surface of the positive electrode member.
The temperature of the electrolytic solution is increased in the vicinity of the surface of the annular treatment region due to heat generated by the electrode reaction, and when the smooth flow of the electrolytic solution is hindered, the temperature of the electrolytic solution is likely to increase.
When the temperature of the electrolytic solution rises, for example, so-called burns tend to occur in the surface treatment in which a film such as an alumite film is formed in the annular treatment region, and there is a possibility that the surface treatment cannot be efficiently and repeatedly performed at a high voltage.
The present invention has been made in view of the above circumstances, and an object thereof is to provide a surface treatment apparatus capable of efficiently and repeatedly performing surface treatment at a high voltage.

本発明による表面処理装置の第1特徴構成は、環状被処理領域を外周面の円周方向に沿って有する円柱状の金属製の被処理物に電気的に接続される陽電極部材又は陰電極部材の一方と、前記外周面及び前記環状被処理領域に対して間隔を隔てて対向する非導電性の内周面を備えた枠部材と、前記外周面のうち前記環状被処理領域を挟んだ両側夫々と前記内周面との隙間をシールすることにより、前記環状被処理領域に沿った電解液通路を形成可能な非導電性の弾性シール材と、先端部が前記電解液通路の中に入り込むように前記被処理物の側に向けて突設してある棒状の陽電極部材又は陰電極部材の他方と、前記電解液通路に沿って電解液を通流させる電解液通流手段とを備えている点にある。 A first characteristic configuration of a surface treatment apparatus according to the present invention is a positive electrode member or a negative electrode that is electrically connected to a cylindrical metal workpiece having an annular treatment region along the circumferential direction of the outer peripheral surface. One of the members, a frame member having a non-conductive inner peripheral surface facing the outer peripheral surface and the annular processing region with a space therebetween, and sandwiching the annular processing region among the outer peripheral surfaces By sealing a gap between each of the both sides and the inner peripheral surface, a non-conductive elastic sealing material capable of forming an electrolyte passage along the annular processing region, and a tip portion in the electrolyte passage The other of the rod-shaped positive electrode member or negative electrode member protruding toward the object to be processed so as to enter, and the electrolyte solution flow means for flowing the electrolyte solution along the electrolyte passage It is in the point to have.

本構成であれば、枠部材が被処理物の外周面及び環状被処理領域に対して間隔を隔てて対向する非導電性の内周面を備えているので、表面処理時において、金属成分や非金属成分が枠部材の内周面に析出することがない。
また、棒状の陽電極部材又は陰電極部材の他方を突設してあるので、陽電極部材又は陰電極部材の他方の表面積を従来に比べて小さくして、金属成分や非金属成分などの析出成分の陽電極部材又は陰電極部材の他方に対する付着面積を小さくすることができ、析出成分の陽電極部材又は陰電極部材の他方に対する付着強度を弱めることができる。
そして、棒状の陽電極部材又は陰電極部材の他方を先端部が電解液通路の中に入り込むように被処理物の側に向けて突設してあるので、棒状の陽電極部材又は陰電極部材の他方に堆積した付着強度が弱い析出成分を、電解液通路に沿って通流する電解液の勢いで押し流して棒状の陽電極部材又は陰電極部材の他方から取り除き易くなり、棒状の陽電極部材又は陰電極部材の他方に堆積した析出成分が大きく成長し難い。
したがって、電解液通路における電解液の円滑な通流を長期に亘って確保して、環状被処理領域の表面近傍における温度上昇を長期に亘って抑制することができる。
よって、本構成の表面処理装置であれば、表面処理を高い電圧で能率良く繰り返し行うことができる。
In this configuration, the frame member has a non-conductive inner peripheral surface that is opposed to the outer peripheral surface of the object to be processed and the annular processing region with a space therebetween. Nonmetallic components do not precipitate on the inner peripheral surface of the frame member.
In addition, since the other of the rod-shaped positive electrode member or negative electrode member is projected, the surface area of the other of the positive electrode member or negative electrode member is made smaller than before, so that metal components and non-metal components are deposited. The adhesion area of the component to the other of the positive electrode member or the negative electrode member can be reduced, and the adhesion strength of the deposited component to the other of the positive electrode member or the negative electrode member can be weakened.
And since the other end of the rod-shaped positive electrode member or the negative electrode member is projected toward the object to be processed so that the tip portion enters the electrolyte passage, the rod-shaped positive electrode member or the negative electrode member The deposited component having a weak adhesion strength deposited on the other side of the electrode is easily removed from the other of the rod-shaped positive electrode member or the negative electrode member by the force of the electrolyte flowing along the electrolyte passage, and the rod-shaped positive electrode member Or the deposited component deposited on the other of the negative electrode members is difficult to grow greatly.
Therefore, a smooth flow of the electrolytic solution in the electrolytic solution passage can be ensured over a long period of time, and a temperature increase in the vicinity of the surface of the annular processing region can be suppressed over a long period of time.
Therefore, with the surface treatment apparatus of this configuration, the surface treatment can be efficiently and repeatedly performed at a high voltage.

本発明の第2特徴構成は、前記環状被処理領域に向けて開口する複数の電解液供給ノズルと、前記枠部材の前記内周面に一定の溝幅で形成された周溝とを備え、前記電解液供給ノズルの夫々が、前記周溝の溝内に溝周方向に互いに間隔を隔てて配設され、前記周溝のうちの、隣り合う電解液供給ノズルどうしの間の周溝部分が、電解液排出流路として形成され、前記隣り合う電解液供給ノズルどうしの間隔を、ノズル先端箇所において最も狭くなるように設定してある点にある。   The second characteristic configuration of the present invention comprises a plurality of electrolyte supply nozzles that open toward the annular region to be processed, and a peripheral groove formed with a constant groove width on the inner peripheral surface of the frame member, Each of the electrolyte solution supply nozzles is disposed in the groove of the circumferential groove so as to be spaced apart from each other in the circumferential direction of the groove, and a circumferential groove portion between adjacent electrolyte solution supply nozzles of the circumferential grooves is provided. , Which is formed as an electrolyte solution discharge channel, and the distance between the adjacent electrolyte solution supply nozzles is set to be the narrowest at the nozzle tip portion.

例えばアルマイト被膜などの被膜を環状被処理領域に形成する表面処理においては、反応面近傍の電解液の温度が上昇すると硬度が低い被膜が形成され、目標硬度の被膜を形成できないおそれがある。
本構成の表面処理装置であれば、被膜を環状被処理領域に形成する表面処理において、目標硬度の被膜を均一に形成し易い。
For example, in the surface treatment in which a film such as an alumite film is formed in the annular processing region, when the temperature of the electrolytic solution in the vicinity of the reaction surface rises, a film having a low hardness may be formed and a film having a target hardness may not be formed.
With the surface treatment apparatus of this configuration, it is easy to form a film having a target hardness uniformly in the surface treatment for forming the film in the annular processing region.

すなわち、本構成の表面処理装置は、枠部材の内周面に周溝が一定の溝幅で形成され、電解液供給ノズルの夫々が、その周溝の溝内に溝周方向に互いに間隔を隔てて配設されている。
このため、電解液通路を通流する電解液の温度分布を均一化して、環状被処理領域に形成された被膜の硬度の均一化を図り易い。
That is, in the surface treatment apparatus of this configuration, the circumferential groove is formed with a constant groove width on the inner circumferential surface of the frame member, and each of the electrolyte supply nozzles is spaced from each other in the circumferential direction of the groove in the circumferential groove. They are spaced apart.
For this reason, it is easy to make uniform the temperature distribution of the electrolyte flowing through the electrolyte passage and to make the hardness of the coating formed in the annular processing region uniform.

また、周溝のうちの、隣り合う電解液供給ノズルどうしの間の周溝部分が、電解液排出流路として形成されている。
このため、電解液通路に沿って旋回するように通流している電解液を、電解液供給ノズルどうしの間の周溝部分(電解液排出流路)に遠心力で勢い良く流入させることができる。
Moreover, the circumferential groove part between adjacent electrolyte solution supply nozzles of the circumferential groove is formed as an electrolyte solution discharge flow path.
For this reason, the electrolytic solution flowing so as to swirl along the electrolytic solution passage can be vigorously flowed into the peripheral groove portion (electrolytic solution discharge flow channel) between the electrolytic solution supply nozzles by centrifugal force. .

さらに、隣り合う電解液供給ノズルどうしの間隔を、ノズル先端箇所において最も狭くなるように設定してある。
このため、電解液排出流路の流路断面積をノズル先端箇所において絞って、排出される電解液の流速を速くすることができる。
ノズル先端箇所の近傍における電解液の流速を速くすると、その流速が速い電解液の流れに随伴する流れ(随伴流)により、ノズル先端箇所の近傍における温度が高い電解液の滞留を防止することができ、電解液通路の温度が高い電解液を電解液供給ノズルから供給される温度が低い電解液に迅速に置き換え易い。
Furthermore, the interval between adjacent electrolyte supply nozzles is set to be the narrowest at the nozzle tip.
For this reason, the flow area of the electrolyte solution can be increased by narrowing the channel cross-sectional area of the electrolyte solution discharge channel at the tip of the nozzle.
When the flow rate of the electrolyte near the nozzle tip is increased, the flow accompanying the flow of the electrolyte having a high flow rate (the accompanying flow) can prevent the high temperature electrolyte from staying near the nozzle tip. In addition, it is easy to quickly replace an electrolytic solution having a high temperature in the electrolytic solution passage with an electrolytic solution having a low temperature supplied from the electrolytic solution supply nozzle.

したがって、被膜の硬度の均一化を図りながら、電解液通路の電解液の温度上昇を抑制することができ、目標硬度の被膜を均一に形成することができる。
また、電解液通路を通流している電解液の温度上昇を抑制して、熱による被膜の溶融も防止することができる。
Therefore, the temperature rise of the electrolyte solution in the electrolyte passage can be suppressed while the hardness of the coating film is made uniform, and the coating film having the target hardness can be formed uniformly.
Moreover, the temperature rise of the electrolyte solution flowing through the electrolyte passage can be suppressed, and the melting of the coating film due to heat can be prevented.

本発明の第2特徴構成は、前記棒状の陽電極部材又は陰電極部材の他方の複数を前記電解液通路の周方向に沿って分散配置してある点にある。   The second characteristic configuration of the present invention is that a plurality of the other of the rod-shaped positive electrode member or the negative electrode member is distributed along the circumferential direction of the electrolyte passage.

本構成であれば、棒状の陽電極部材又は陰電極部材の他方と環状被処理領域との間に発生する電場の強さを環状被処理領域に沿って分散させて、均質な被膜を形成し易い。   With this configuration, the electric field generated between the other of the rod-shaped positive electrode member or negative electrode member and the annular treatment area is dispersed along the annular treatment area to form a uniform film. easy.

本発明の第3特徴構成は、前記棒状の陽電極部材又は陰電極部材の他方を、その長手方向が前記外周面に対して直交する方向となるように突設してある点にある。   The third characteristic configuration of the present invention is that the other of the rod-shaped positive electrode member or the negative electrode member is projected so that its longitudinal direction is perpendicular to the outer peripheral surface.

本構成であれば、棒状の陽電極部材又は陰電極部材の他方と、その棒状の陽電極部材又は陰電極部材の他方に対して左右両側に位置する環状被処理領域部分との間に電場を左右対称に発生させて、均質な被膜を形成し易い。   In this configuration, an electric field is generated between the other of the rod-shaped positive electrode member or the negative electrode member and the annular processed region portions located on the left and right sides with respect to the other of the rod-shaped positive electrode member or the negative electrode member. It is generated symmetrically and it is easy to form a uniform film.

本発明の第4特徴構成は、前記棒状の陽電極部材又は陰電極部材の他方の外周面を凹凸面に形成してある点にある。   The 4th characteristic structure of this invention exists in the point which has formed the other outer peripheral surface of the said rod-shaped positive electrode member or negative electrode member in the uneven surface.

本構成であれば、棒状の陽電極部材又は陰電極部材の他方の表面積を大きくすることができるので大きな電流を流すことができるようになり、所望厚さの被膜を短い時間で能率良く形成し易い。   With this configuration, the other surface area of the rod-shaped positive electrode member or negative electrode member can be increased, so that a large current can flow, and a film having a desired thickness can be efficiently formed in a short time. easy.

本発明の第5特徴構成は、前記棒状の陽電極部材又は陰電極部材の他方における先端部の形状を凸曲面状に形成してある点にある。   The fifth characteristic configuration of the present invention is that the shape of the tip of the other of the rod-shaped positive electrode member or the negative electrode member is formed in a convex curve shape.

本構成であれば、被処理物に近い先端部に電流が集中し難くなり、スパークが発生し難いので、均質な被膜を形成し易い。   With this configuration, it is difficult for current to concentrate on the tip portion close to the object to be processed, and it is difficult for sparks to be generated, so that it is easy to form a uniform film.

表面処理装置(陽極酸化処理装置)の概略図である。It is the schematic of a surface treatment apparatus (anodization processing apparatus). (a)は図1のII−II線矢視における第2電極部の平面図、(b)は第2電極部の拡大平面図である。(A) is a top view of the 2nd electrode part in the II-II line arrow of FIG. 1, (b) is an enlarged plan view of a 2nd electrode part. (a)は陰電極部材の固定構造を示す断面図、(b)は(a)におけるIII b−III b線矢視側面図である。(A) is sectional drawing which shows the fixed structure of a negative electrode member, (b) is the IIIb-IIIb arrow directional side view in (a). 第2電極部の電解液供給ノズル部分を示す断面図である。It is sectional drawing which shows the electrolyte solution supply nozzle part of a 2nd electrode part. 第2電極部の内周側を示す側面図である。It is a side view which shows the inner peripheral side of a 2nd electrode part. 第2電極部の弾性シール材がピストンの外周面から離間している状態を示す断面図である。It is sectional drawing which shows the state from which the elastic sealing material of the 2nd electrode part is spaced apart from the outer peripheral surface of a piston. 第2電極部の弾性シール材がピストンの外周面に圧接されている状態を示す断面図である。It is sectional drawing which shows the state by which the elastic sealing material of a 2nd electrode part is press-contacted to the outer peripheral surface of a piston. 排出面積比率(S1/S2)と、環状被処理領域に形成されたアルマイト被膜の硬度(Hk)との相関関係を示す図表である。It is a graph which shows correlation with discharge area ratio (S1 / S2) and the hardness (Hk) of the alumite film formed in the cyclic | annular to-be-processed area | region. 排出面積比率(S1/S2)と、電解液排出流路を通して排出される電解液の上昇温度ΔTとの相関関係を示す図表である。It is a graph which shows correlation with discharge | emission area ratio (S1 / S2) and rising temperature (DELTA) T of the electrolyte solution discharged | emitted through an electrolyte solution discharge flow path. 第2実施形態の表面処理装置(陽極酸化処理装置)における陰電極部材を示す側面図である。It is a side view which shows the negative electrode member in the surface treatment apparatus (anodization apparatus) of 2nd Embodiment.

以下に本発明の実施の形態を図面に基づいて説明する。
〔第1実施形態〕
図1〜図7は、本発明による表面処理装置の一例としての陽極酸化処理装置を示している。この陽極酸化処理装置は、金属製の被処理物の一例としてのアルミニウム合金製ピストンAのピストンリング溝A1に対して、その表面にアルマイト被膜を形成する陽極酸化処理を行うものである。
Embodiments of the present invention will be described below with reference to the drawings.
[First Embodiment]
1 to 7 show an anodizing apparatus as an example of a surface treating apparatus according to the present invention. This anodizing apparatus performs anodizing treatment for forming an alumite film on the surface of a piston ring groove A1 of an aluminum alloy piston A as an example of a metal workpiece.

具体的には、円柱状のピストンAの頂部からスカート部にかけて形成された3個のピストンリング溝A1,A2,A3のうちの、頂部側のピストンリング(コンプレッションリング)溝A1の表面を含む外周面(以下、ピストン外周面という)Bに対して陽極酸化処理を実施する。
ピストンリング溝A1が、ピストン外周面Bに有する環状被処理領域としての周溝に相当している。
Specifically, the outer periphery including the surface of the piston ring (compression ring) groove A1 on the top side of the three piston ring grooves A1, A2 and A3 formed from the top to the skirt of the cylindrical piston A Anodizing is performed on the surface (hereinafter referred to as piston outer peripheral surface) B.
The piston ring groove A1 corresponds to a circumferential groove as an annular process area on the piston outer peripheral surface B.

陽極酸化処理装置は、図1に示すように、電解液槽1と電解液供給部2と酸化処理部3と通電部4とを有する。
電解液槽1は、塩化ビニル製又はステンレス鋼製で、上端が開口する容器状のものであり、酸化処理部3を通過した後の自然流下する電解液を受け止めて回収するとともに、電解液供給部2に還流するための還流路5が設けられている。
As shown in FIG. 1, the anodizing apparatus includes an electrolytic solution tank 1, an electrolytic solution supply unit 2, an oxidation processing unit 3, and an energization unit 4.
The electrolytic solution tank 1 is made of vinyl chloride or stainless steel, and has a container shape with an open top. The electrolytic solution tank 1 receives and collects the electrolytic solution that naturally flows after passing through the oxidation treatment unit 3 and supplies the electrolytic solution. A reflux path 5 for refluxing the part 2 is provided.

電解液供給部2は、電解液槽1から還流された電解液を冷却するための冷却槽6と、冷却槽6の電解液を酸化処理部3に供給するための供給路7と、供給路7に設けてある供給ポンプ8と、電解液が所定のタイミングで酸化処理部3に供給されるように供給ポンプ8の運転を制御する供給制御部9とを有している。   The electrolytic solution supply unit 2 includes a cooling tank 6 for cooling the electrolytic solution refluxed from the electrolytic solution tank 1, a supply path 7 for supplying the electrolytic solution in the cooling tank 6 to the oxidation treatment unit 3, and a supply path 7 and a supply control unit 9 for controlling the operation of the supply pump 8 so that the electrolytic solution is supplied to the oxidation treatment unit 3 at a predetermined timing.

冷却槽6には、回収された電解液を冷却するための冷却機10と、電解液が所定温度に冷却されるように、温度センサ11による電解液温度の検出情報に基づいて、冷却機10の運転を制御する冷却制御部12とが設けられている。   The cooling tank 6 includes a cooler 10 for cooling the recovered electrolyte solution, and a cooler 10 based on detection information of the electrolyte temperature by the temperature sensor 11 so that the electrolyte solution is cooled to a predetermined temperature. And a cooling control unit 12 for controlling the operation of the above.

通電部4は、酸化処理部3に通電するものである。この通電部4は電流密度を調整できるように電流制御手段を持つものとするのが好ましい。電流制御手段は電流計、電圧計、整流器等で構成された従来公知のものを用いることができる。   The energization unit 4 energizes the oxidation treatment unit 3. The energization section 4 preferably has current control means so that the current density can be adjusted. As the current control means, a conventionally known one composed of an ammeter, a voltmeter, a rectifier or the like can be used.

酸化処理部3は、第1電極(陽極)部13と第2電極(陰極)部14とを有する。
第1電極部13は、導電性を備えた銅やステンレス鋼などの金属製の陽電極部材15と、陽電極部材15を第2電極部14に対して昇降させる昇降装置16とを備えている。
陽電極部材15は、ピストンAを保持する保持具と兼用してあって、通電部4の陽極端子4aに電気的に接続されており、ピストンAを保持することにより当該ピストンAに電気的に接続される。
The oxidation processing unit 3 includes a first electrode (anode) unit 13 and a second electrode (cathode) unit 14.
The first electrode portion 13 includes a positive electrode member 15 made of metal such as copper or stainless steel having conductivity, and an elevating device 16 that moves the positive electrode member 15 up and down with respect to the second electrode portion 14. .
The positive electrode member 15 is also used as a holder for holding the piston A, and is electrically connected to the anode terminal 4a of the energizing portion 4, and is electrically connected to the piston A by holding the piston A. Connected.

保持具(陽電極部材)15は、ピストンAの内周面に係脱自在な係止爪(図示せず)をその下端部に備えている。この係止爪をピストンAの内周面に係止することにより、ピストンAをその軸芯が垂直方向に沿う姿勢で、かつ、電気的に接続した状態で保持する。   The holder (positive electrode member) 15 includes a locking claw (not shown) that can be freely engaged with and disengaged from the inner peripheral surface of the piston A at its lower end. By locking the locking claw to the inner peripheral surface of the piston A, the piston A is held in a posture in which the axial center is along the vertical direction and is electrically connected.

第2電極部14は、図2(a)に示すように、外形が平面視で円形に形成され、ピストンAをその軸芯を上下方向に沿わせた姿勢で入り込ませる平面視で円形のピストン挿入孔25が同芯状に形成されている。   As shown in FIG. 2 (a), the second electrode portion 14 is formed in a circular shape when viewed from above, and has a circular shape when viewed in a plan view in which the piston A is inserted in a posture in which its axial center is along the vertical direction. The insertion hole 25 is formed concentrically.

第2電極部14は、図1〜図3に示すように、丸棒状の複数の陰電極部材41を固定してある枠部材17と、枠部材17の上下に配置した固定板18,19と、支持基盤20とを有し、互いにボルト連結してある。各陰電極部材41は、白金(Pt)又は導電性のステンレス鋼(SUS)で形成してある。
陰電極部材41の数は4〜20本が望ましく、本実施形態では、14本の陰電極部材41を枠部材17の周方向に沿って分散配置してある。
枠部材17、固定板18,19及び支持基盤20は、いずれも、塩化ビニル樹脂などの非導電性材料(絶縁体)で形成されている。
As shown in FIGS. 1 to 3, the second electrode portion 14 includes a frame member 17 to which a plurality of round electrode members 41 are fixed, and fixing plates 18 and 19 disposed above and below the frame member 17. The support base 20 is connected to each other by bolts. Each negative electrode member 41 is formed of platinum (Pt) or conductive stainless steel (SUS).
The number of negative electrode members 41 is desirably 4 to 20, and in the present embodiment, 14 negative electrode members 41 are dispersedly arranged along the circumferential direction of the frame member 17.
The frame member 17, the fixing plates 18, 19 and the support base 20 are all formed of a nonconductive material (insulator) such as vinyl chloride resin.

枠部材17は、図1,図3,図4に示すように、上側固定板18の下面外周側を上向きに凹入させてある環状の上向き凹面部21と、下側固定板19の上面外周側を下向きに凹入させてある環状の下向き凹面部22との間に嵌合されて、互いにボルト連結してある。   As shown in FIGS. 1, 3, and 4, the frame member 17 includes an annular upward concave surface portion 21 in which the lower surface outer peripheral side of the upper fixing plate 18 is recessed upward, and an upper surface outer periphery of the lower fixing plate 19. It is fitted between an annular downward concave surface portion 22 having a side recessed downward and is bolted to each other.

枠部材17は、図1に示すように、上側の第1枠板23と下側の第2枠板24との二枚の枠板をボルト連結することにより構成してあり、図3,図5に示すように、第1枠板23と第2枠板24との間に陰電極部材41を挟み込んで固定してある。   As shown in FIG. 1, the frame member 17 is configured by connecting two frame plates, that is, an upper first frame plate 23 and a lower second frame plate 24, as shown in FIGS. As shown in FIG. 5, the negative electrode member 41 is sandwiched and fixed between the first frame plate 23 and the second frame plate 24.

図4〜図6に示すように、枠部材17は、その内周面(以下、枠板内周面という)31に、一定の溝幅で形成された周溝26を備えている。
周溝26は、第1枠板23と第2枠板24とを空間を隔てて対向させる対向板部27,28と、対向板部27,28の内周側に沿ってピストン挿通孔25の側に突出する鍔板部29,30とを環状に形成して、第1枠板23及び第2枠板24のピストン挿入孔25の側に設けてある。
As shown in FIGS. 4 to 6, the frame member 17 includes a circumferential groove 26 formed with a constant groove width on an inner circumferential surface (hereinafter referred to as a frame plate inner circumferential surface) 31.
The circumferential grooves 26 are opposed plate portions 27, 28 that make the first frame plate 23 and the second frame plate 24 face each other with a space therebetween, and the piston insertion holes 25 along the inner peripheral side of the opposed plate portions 27, 28. Side plate portions 29 and 30 projecting to the side are formed in an annular shape and provided on the piston insertion hole 25 side of the first frame plate 23 and the second frame plate 24.

各鍔板部29,30の内周面で形成される枠板内周面31の内側がピストン挿通孔25として形成されている。
したがって、枠部材17は、ピストン外周面B及びピストンリング溝A1に対して全周に亘って一定間隔を隔てて対向する非導電性の円環状内周面として形成された枠板内周面31を備えている。
The inner side of the inner peripheral surface 31 of the frame plate formed by the inner peripheral surfaces of the flange plates 29 and 30 is formed as a piston insertion hole 25.
Therefore, the frame member 17 is a frame plate inner peripheral surface 31 formed as a non-conductive annular inner peripheral surface that is opposed to the piston outer peripheral surface B and the piston ring groove A1 at a predetermined interval over the entire periphery. It has.

図1に示すように、下側固定板19には、ピストン挿通孔25と同径で、かつ、同芯の円形凹面部32と、軸芯を上下方向に沿わせた姿勢のピストンAの頂面を載置支持するピストン載置部35とを設けてある。
下側固定板19と支持基盤20とに亘って、電解液の供給路7に接続される接続流路33と、円形凹面部32に溜まった電解液を自然流下により電解液槽1に排出する排出孔34とが設けられている。
As shown in FIG. 1, the lower fixing plate 19 has the same diameter as the piston insertion hole 25, the concentric circular concave surface portion 32, and the top of the piston A in a posture in which the shaft core is vertically aligned. A piston mounting portion 35 for mounting and supporting the surface is provided.
Over the lower fixing plate 19 and the support base 20, the connection flow path 33 connected to the electrolytic solution supply path 7 and the electrolytic solution accumulated in the circular concave surface portion 32 are discharged into the electrolytic solution tank 1 by natural flow. A discharge hole 34 is provided.

したがって、図1に示すように、軸芯が鉛直方向に沿う姿勢で電気的に接続した状態で保持具(陽電極部材)15に保持されたピストンAが、ピストン挿通孔25に挿通されて、その頂面がピストン載置部35に載置されることにより、図3,図4に示すように、ピストン外周面Bと枠板内周面31との間に全周に亘って一定間隔の隙間Cを有する同芯状に位置決めされる。   Therefore, as shown in FIG. 1, the piston A held by the holder (positive electrode member) 15 with the shaft core electrically connected in a posture along the vertical direction is inserted through the piston insertion hole 25, By placing the top surface on the piston mounting portion 35, as shown in FIGS. 3 and 4, a constant interval is provided between the piston outer peripheral surface B and the frame plate inner peripheral surface 31 over the entire circumference. It is positioned concentrically with a gap C.

枠部材17における枠板内周面31の側には、図1,図3〜図7に示すように、上下二個の非導電性の環状の弾性シール材40を全周に亘って上下に間隔を隔てて抜け止め状態で、かつ、先端部44が枠板内周面31よりもピストン外周面Bの側に突出しないように装着してある。   As shown in FIGS. 1 and 3 to 7, on the frame member inner peripheral surface 31 side of the frame member 17, two upper and lower non-conductive annular elastic sealing materials 40 are vertically moved over the entire circumference. The front end portion 44 is mounted so as not to come off at an interval and so as not to protrude from the inner peripheral surface 31 of the frame plate to the piston outer peripheral surface B side.

各弾性シール材40は、ゴムなどの非導電性材料(絶縁体)で円環状に形成してあり、図7に示すように、その先端部44がピストン外周面Bに圧接されるように伸長させて、ピストン外周面Bのうち周溝A1を挟んだ両側夫々と枠板内周面31との隙間Cをシールすることにより、周溝A1に沿った環状の電解液通路45を形成可能である。   Each elastic sealing member 40 is formed in an annular shape with a non-conductive material (insulator) such as rubber, and as shown in FIG. 7, it extends so that its tip 44 is pressed against the piston outer peripheral surface B. The annular electrolyte passage 45 along the circumferential groove A1 can be formed by sealing the gap C between the both sides of the piston outer circumferential surface B across the circumferential groove A1 and the inner peripheral surface 31 of the frame plate. is there.

各弾性シール材40は、その外周側に向けて開口する凹入部42を全周に亘って一連に形成して、上下の側壁部43と、ピストン外周面Bに対して接触させる先端部44とを一体に備えた横向きU字状の横断面形状に形成してある。   Each elastic sealing material 40 is formed with a series of recessed portions 42 that open toward the outer peripheral side thereof over the entire circumference, and upper and lower side wall portions 43 and a tip end portion 44 that is brought into contact with the piston outer peripheral surface B. Are formed in a transverse U-shaped transverse cross-sectional shape.

図1,図6,図7に示すように、各弾性シール材40の外周側に加圧流体としての加圧空気を同時に供給することにより、これら弾性シール材40の内周側(先端部44)を全周に亘ってピストン外周面Bに圧接し、かつ、圧接を解除自在な加圧機構51を設けてある。   As shown in FIGS. 1, 6, and 7, by simultaneously supplying pressurized air as a pressurized fluid to the outer peripheral side of each elastic sealing material 40, the inner peripheral side (tip portion 44) of these elastic sealing materials 40. ) Is press-contacted to the piston outer peripheral surface B over the entire circumference, and a pressurizing mechanism 51 capable of releasing the press-contact is provided.

加圧機構51は、加圧空気の供給及び排出が自在な空気給排装置52と、空気給排装置52の空気給排動作を制御する給排制御部53と、弾性シール材40の凹入部42の夫々に連通する空気給排路54と、空気給排装置52の空気給排管55と空気給排路54とを接続する管継手56とを有する。   The pressurizing mechanism 51 includes an air supply / discharge device 52 that can freely supply and discharge pressurized air, a supply / discharge control unit 53 that controls the air supply / discharge operation of the air supply / discharge device 52, and a recessed portion of the elastic seal material 40. 42, an air supply / discharge passage 54 communicating with each of the air supply / discharge passages 42, and a pipe joint 56 connecting the air supply / discharge passage 55 of the air supply / discharge device 52 and the air supply / discharge passage 54.

空気給排路54は、第2電極部14の周方向三箇所に設けられ、各空気給排路54毎に空気給排管55に接続して、各弾性シール材40の凹入部42に対して周方向の三箇所から加圧空気を給排自在である。   The air supply / discharge paths 54 are provided at three locations in the circumferential direction of the second electrode portion 14, and are connected to the air supply / discharge pipes 55 for each of the air supply / discharge paths 54, with respect to the recessed portions 42 of the elastic sealing materials 40. Thus, pressurized air can be freely supplied and discharged from three locations in the circumferential direction.

加圧機構51の動作を説明する。
図6に示すようにピストンAがピストン挿通孔25に挿通されてピストン載置部35に載置されると、給排制御部53は、空気給排路54を通して各弾性シール材40の凹入部42の夫々に加圧空気が供給されるように、空気給排装置52を作動させる。
The operation of the pressurizing mechanism 51 will be described.
As shown in FIG. 6, when the piston A is inserted into the piston insertion hole 25 and placed on the piston placement portion 35, the supply / exhaust control portion 53 passes through the air supply / exhaust passage 54 to insert the recessed portion of each elastic seal material 40. The air supply / exhaust device 52 is operated so that pressurized air is supplied to each of 42.

弾性シール材40の凹入部42に加圧空気が供給されると、当該弾性シール材40がピストン外周面Bの側に向けて弾性的に伸長すると共に、先端部44がピストン外周面Bに向けて弾性的に膨出移動して、図7に示すように当該先端部44がピストン外周面Bに圧接される。   When pressurized air is supplied to the recessed portion 42 of the elastic seal material 40, the elastic seal material 40 elastically extends toward the piston outer peripheral surface B, and the tip end portion 44 faces the piston outer peripheral surface B. As shown in FIG. 7, the tip 44 is pressed against the piston outer peripheral surface B.

図7に示すように弾性シール材40の先端部44がピストン外周面Bに圧接されることにより、周溝A1を挟む両側夫々においてピストン外周面Bと枠板内周面31との隙間Cがシールされて周溝A1に沿った環状の電解液通路45が形成される。   As shown in FIG. 7, the tip 44 of the elastic seal material 40 is brought into pressure contact with the piston outer peripheral surface B, so that a gap C between the piston outer peripheral surface B and the frame plate inner peripheral surface 31 is formed on both sides of the peripheral groove A1. Sealed to form an annular electrolyte passage 45 along the circumferential groove A1.

図2(a),図3,図5に示すように、陰電極部材41の夫々は、先端部46aが電解液通路45の中に入り込むようにピストンAの側に向けて突設される電極軸部46と、枠部材17に固定される固定用軸部47と、通電部4の陰極端子4bに電気的に接続される接続軸部48とを備えた真っ直ぐな丸棒状に形成してある。
電極軸部46の先端部46aの形状は、角部を備えない凸曲面形状に形成してある。
As shown in FIGS. 2A, 3, and 5, each of the negative electrode members 41 is an electrode that protrudes toward the piston A so that the tip 46 a enters the electrolyte passage 45. It is formed in a straight round bar shape including a shaft portion 46, a fixing shaft portion 47 that is fixed to the frame member 17, and a connection shaft portion 48 that is electrically connected to the cathode terminal 4 b of the energization portion 4. .
The shape of the tip end portion 46a of the electrode shaft portion 46 is formed in a convex curved surface shape having no corners.

複数の陰電極部材41は、その長手方向(軸芯方向)がピストン外周面Bに対して直交する方向と同じ方向となるように、又は、その直交する方向に対して75度以内の角度範囲で傾斜するように配置するのが望ましい。
本実施形態では、複数の陰電極部材41を、図2(a)に示すように、電極軸部46の長手方向がピストン外周面Bに対して直交する方向となるように、ピストン挿入孔25の中心に対する放射状に配設して、電解液通路45の周方向に沿って等間隔で分散配置してある。
The negative electrode members 41 have an angle range of 75 degrees or less so that the longitudinal direction (axial center direction) is the same direction as the direction orthogonal to the piston outer peripheral surface B. It is desirable to arrange so as to be inclined at
In the present embodiment, the plurality of negative electrode members 41 are connected to the piston insertion holes 25 so that the longitudinal direction of the electrode shaft portion 46 is orthogonal to the piston outer peripheral surface B as shown in FIG. Are arranged radially at equal intervals along the circumferential direction of the electrolyte passage 45.

各陰電極部材41は、図3,図5に示すように電極軸部46が後述する電解液排出流路38の中をピストンAの側に向けて突出し、図2に示すように接続軸部48が枠部材17の外周側に突出するように、固定用軸部47を第1枠板23と第2枠板24との間に嵌合状態で挟み込んで固定されている。   As shown in FIGS. 3 and 5, each negative electrode member 41 has an electrode shaft portion 46 projecting toward the piston A side through an electrolyte discharge flow path 38, which will be described later, and a connecting shaft portion as shown in FIG. The fixing shaft portion 47 is sandwiched and fixed between the first frame plate 23 and the second frame plate 24 so that 48 protrudes to the outer peripheral side of the frame member 17.

各陰電極部材41の接続軸部48は、図2(a)に示すように、通電部4の陰極端子4bに電気的に接続された共通の接続端子板49に電気的に接続されている。
接続端子板49は枠部材17を囲む円環状に形成され、接続軸部48の夫々は、図3
(b)に示すように、接続端子板49と接続端子板49にボルト固定される受け板50との間に挟み込んで、電気的に接続されている。
As shown in FIG. 2A, the connection shaft portion 48 of each negative electrode member 41 is electrically connected to a common connection terminal plate 49 that is electrically connected to the cathode terminal 4 b of the energization portion 4. .
The connection terminal plate 49 is formed in an annular shape surrounding the frame member 17, and each of the connection shaft portions 48 is shown in FIG. 3.
As shown in (b), the connection terminal plate 49 and the receiving plate 50 bolted to the connection terminal plate 49 are sandwiched and electrically connected.

したがって、陰電極部材41の交換に際しては、接続軸部48と接続端子板49との接続を解除して、交換対象の陰電極部材41を第1枠板23と第2枠板24との間から抜き出し、新たな陰電極部材41を第1枠板23と第2枠板24との間に差し込んで接続端子板49に接続することにより、容易に交換することができる。   Therefore, when replacing the negative electrode member 41, the connection between the connection shaft portion 48 and the connection terminal plate 49 is released, and the negative electrode member 41 to be replaced is placed between the first frame plate 23 and the second frame plate 24. It is possible to easily replace the negative electrode member 41 by inserting it between the first frame plate 23 and the second frame plate 24 and connecting it to the connection terminal plate 49.

図2(a),図4,図5に示すように、第1枠板23における対向板部27及び鍔板部29と、第2枠板24における対向板部28及び鍔板部30との間、つまり、周溝26の溝内には、ピストンリング溝A1に向けて開口する複数の電解液供給ノズル36が溝周方向に互いに一定間隔を隔てて配設されている。
電解液供給ノズル36は、陰電極部材41と同じ数を配設するのが望ましく、本実施形態では陰電極部材41と同じ数の14個を配設してある。
As shown in FIG. 2A, FIG. 4, and FIG. 5, the opposing plate portion 27 and the saddle plate portion 29 in the first frame plate 23, and the opposing plate portion 28 and the saddle plate portion 30 in the second frame plate 24. A plurality of electrolyte supply nozzles 36 that open toward the piston ring groove A <b> 1 are arranged at regular intervals in the groove circumferential direction.
It is desirable to dispose the same number of electrolyte supply nozzles 36 as the negative electrode members 41. In the present embodiment, 14 electrolytic electrode supply nozzles 36 having the same number as the negative electrode members 41 are disposed.

図4,図5に示すように、各電解液供給ノズル36は、接続流路33に接続されているとともに、電解液通路45に電解液を供給する供給流路37を備え、この供給流路37がピストンリング溝A1に向けて枠板内周面31に開口している。
電解液供給ノズル36は、図2(a)に示すように、その供給流路37の流路軸芯Xが枠板内周面31の接線に対して5〜75度の角度範囲で傾斜するように設けてあるのが望ましい。
As shown in FIGS. 4 and 5, each electrolyte supply nozzle 36 is connected to the connection flow path 33 and includes a supply flow path 37 for supplying the electrolyte solution to the electrolyte passage 45. 37 opens on the inner peripheral surface 31 of the frame plate toward the piston ring groove A1.
As shown in FIG. 2A, the electrolyte supply nozzle 36 is inclined at an angle range of 5 to 75 degrees with respect to the tangent line of the inner peripheral surface 31 of the flow path axis X of the supply flow path 37. It is desirable to be provided as follows.

図1,図5に示すように、周溝26のうちの、隣り合う電解液供給ノズル36どうしの間の周溝部分、つまり、周方向で隣り合う電解液供給ノズル36の間における上下の対向板部27,28の間の空間及び上下の鍔板部29,30の間の空間が電解液排出流路38として設けられている。   As shown in FIGS. 1 and 5, the circumferential groove portion between adjacent electrolyte solution supply nozzles 36 in the circumferential groove 26, that is, the upper and lower facings between the electrolyte solution supply nozzles 36 adjacent in the circumferential direction. A space between the plate portions 27 and 28 and a space between the upper and lower plate portions 29 and 30 are provided as the electrolyte discharge flow path 38.

各電解液供給ノズル36は、電解液が電解液通路45に沿って通流するように、枠板内周面31の接線に対して傾斜する方向から電解液通路45に電解液を供給できるように配設されている。   Each electrolytic solution supply nozzle 36 can supply the electrolytic solution to the electrolytic solution passage 45 from a direction inclined with respect to the tangent to the inner peripheral surface 31 of the frame plate so that the electrolytic solution flows along the electrolytic solution passage 45. It is arranged.

したがって、これらの電解液供給ノズル36を備えた電解液供給部2が、電解液通路45に沿って電解液を通流させる電解液通流手段として設けられ、図5において矢印aで示すように、電解液は電極軸部46の表面を取り巻くように通流するので、電極軸部46に堆積した付着強度が弱い析出金属を電解液の勢いで押し流して取り除き易い。   Therefore, the electrolytic solution supply unit 2 including these electrolytic solution supply nozzles 36 is provided as an electrolytic solution flow means for flowing the electrolytic solution along the electrolytic solution passage 45, as shown by an arrow a in FIG. Since the electrolytic solution flows so as to surround the surface of the electrode shaft portion 46, it is easy to remove the deposited metal deposited on the electrode shaft portion 46 with low adhesion strength by the force of the electrolytic solution.

電極軸部46に堆積した析出金属を取り除き易いので、堆積した析出金属がピストン外周面Bや周溝A1に接触することによるスパークが発生し難く、形成したアルマイト被膜がスパークにより溶解して処理品質が低下するおそれが少ない。   Since it is easy to remove the deposited metal deposited on the electrode shaft portion 46, it is difficult for sparks to be generated due to the deposited deposited metal coming into contact with the piston outer peripheral surface B or the circumferential groove A1, and the formed alumite film is dissolved by the spark and processed quality. Is less likely to decrease.

図2(a)に示すように、周方向で隣り合う電解液供給ノズル36の間の位置に、下側の対向板部28,下側固定板19及び支持基盤20に亘って貫通する貫通孔39が形成され、電解液排出流路38の電解液はこれらの貫通孔39から自然流下して電解液槽1に排出される。   As shown in FIG. 2A, a through-hole penetrating the lower opposing plate portion 28, the lower fixing plate 19 and the support base 20 at a position between the electrolyte supply nozzles 36 adjacent in the circumferential direction. 39 is formed, and the electrolytic solution in the electrolytic solution discharge flow path 38 naturally flows down from these through holes 39 and is discharged to the electrolytic solution tank 1.

また、電解液供給ノズル36は平面視で矩形状に形成され、隣り合う電解液供給ノズル36どうしの間隔を、ノズル先端箇所において最も狭くなるように設定して、電解液排出流路38の流路断面積をノズル先端箇所において絞ってある。   The electrolyte supply nozzle 36 is formed in a rectangular shape in plan view, and the interval between the adjacent electrolyte supply nozzles 36 is set to be the narrowest at the tip of the nozzle, so that the flow of the electrolyte discharge channel 38 can be reduced. The road cross-sectional area is narrowed at the tip of the nozzle.

すなわち、図2(b)に示すように、互いに隣り合う二つの電解液供給ノズル36のうちの、一方の電解液供給ノズル36におけるノズル先端箇所のノズル先端面36aとノズル側面36bとが交差する角部58から他方の電解液供給ノズル36までの最短距離Lを、一方の電解液供給ノズル36における他の部分(ノズル側面36bやノズル後端面36c)から他方の電解液供給ノズル36までの距離よりも短くなるように設定してある。   That is, as shown in FIG. 2B, the nozzle tip surface 36a and the nozzle side surface 36b of the nozzle tip portion of one of the two electrolyte solution supply nozzles 36 adjacent to each other intersect each other. The shortest distance L from the corner 58 to the other electrolyte supply nozzle 36 is the distance from the other part (the nozzle side surface 36b and the nozzle rear end surface 36c) of the one electrolyte supply nozzle 36 to the other electrolyte supply nozzle 36. It is set to be shorter.

本実施形態の陽極酸化処理装置は、陰電極部材41に堆積した析出金属が大きく成長し難いので、析出金属の析出厚さが陰電極部材41の交換が必要な厚さになるまでの電極使用時間が、ピストンAの外周面B及び周溝A1に対して間隔を隔てて対向する環状の内周面を有する陰電極部材を備えた従来の陽極酸化処理装置に比べて、略2倍になった。   In the anodizing apparatus of this embodiment, the deposited metal deposited on the negative electrode member 41 is large and difficult to grow. Therefore, the electrode is used until the deposited thickness of the deposited metal reaches a thickness that requires replacement of the negative electrode member 41. The time is approximately twice as long as that of a conventional anodizing apparatus having a negative electrode member having an annular inner peripheral surface facing the outer peripheral surface B and the peripheral groove A1 of the piston A with a space therebetween. It was.

また、表1に示すように、膜厚が15μmのアルマイト被膜を形成する場合、特許文献1に開示された従来の陽極酸化処理装置に比べて、ヤケ電圧が50V以上高くなり、設定電圧を30V以上高くすることにより、処理時間を30%以上短縮することができた。   As shown in Table 1, when an alumite film having a film thickness of 15 μm is formed, the burn voltage is 50 V or more higher than the conventional anodizing apparatus disclosed in Patent Document 1, and the set voltage is 30 V. By increasing the above, the processing time could be shortened by 30% or more.

Figure 0005522482
Figure 0005522482

図8は、排出流路断面積S1と供給流路断面積S2との比である排出面積比率(S1/S2)と、周溝A1に形成されたアルマイト被膜の硬度(Hk)との相関関係を示す図表である。
排出流路断面積S1は、電解液排出流路38のうちの、隣り合う電解液供給ノズル36どうしの間のノズル先端箇所における最小の流路断面積を合計したものである。
供給流路断面積S2は、各電解液供給ノズル36における供給流路37の流路断面積を合計したものである。
FIG. 8 shows the correlation between the discharge area ratio (S1 / S2), which is the ratio of the discharge channel cross-sectional area S1 and the supply channel cross-sectional area S2, and the hardness (Hk) of the alumite coating formed in the circumferential groove A1. It is a chart which shows.
The discharge channel cross-sectional area S1 is the sum of the minimum channel cross-sectional areas at the nozzle tip positions between the adjacent electrolyte solution supply nozzles 36 in the electrolyte solution discharge channel 38.
The supply channel cross-sectional area S2 is the sum of the channel cross-sectional areas of the supply channels 37 in the electrolyte solution supply nozzles 36.

図9は、排出面積比率(S1/S2)と、貫通孔39を流下する電解液の上昇温度ΔTとの相関関係を示す図表である。
上昇温度ΔTは、電解液の供給流路37への供給温度から上昇した温度である。
FIG. 9 is a chart showing a correlation between the discharge area ratio (S1 / S2) and the rising temperature ΔT of the electrolyte flowing down the through hole 39.
The rising temperature ΔT is a temperature that has risen from the supply temperature of the electrolyte to the supply flow path 37.

図9から、排出面積比率(S1/S2)が大きくなるほど、つまり、排出流路断面積S1が供給流路断面積S2よりも大きくなるほど、熱の回収率が高くなることがわかる。この結果、電解液通路45の電解液の温度上昇が抑制される。
したがって、図8に示すように、排出面積比率(S1/S2)が大きくなるほど、硬度が高いアルマイト被膜が形成されることが分かる。
FIG. 9 indicates that the heat recovery rate increases as the discharge area ratio (S1 / S2) increases, that is, as the discharge flow path cross-sectional area S1 becomes larger than the supply flow path cross-sectional area S2. As a result, the temperature rise of the electrolytic solution in the electrolytic solution passage 45 is suppressed.
Therefore, as shown in FIG. 8, it can be seen that as the discharge area ratio (S1 / S2) increases, an alumite film having higher hardness is formed.

〔第2実施形態〕
図10は、本発明による表面処理装置(陽極酸化処理装置)の別実施形態における陰電極部材41を示す。
本実施形態では、電極軸部46の表面積が大きくなるように、その外周面に凸曲面と凹曲面とを軸芯方向に交互に備えた凹凸面57を形成してある。凸曲面と凹曲面は電極軸部46の軸芯周りで螺旋状に形成してある。
その他の構成は第1実施形態と同様である。
[Second Embodiment]
FIG. 10 shows a negative electrode member 41 in another embodiment of the surface treatment apparatus (anodizing apparatus) according to the present invention.
In the present embodiment, an uneven surface 57 having convex and concave curved surfaces alternately in the axial direction is formed on the outer peripheral surface thereof so that the surface area of the electrode shaft portion 46 is increased. The convex curved surface and the concave curved surface are formed in a spiral shape around the axis of the electrode shaft portion 46.
Other configurations are the same as those of the first embodiment.

〔その他の実施形態〕
1.本発明による表面処理装置は、被処理物の外周面に有する凸面状(山状)や平面状の環状被処理領域に対して表面処理を行うものであっても良い。
2.本発明による表面処理装置は、金属製の被処理物に電気的に接続される陰電極部材と、先端部が電解液通路の中に入り込むように被処理物の側に向けて突設してある棒状の陽電極部材とを備えていてもよい。
3.本発明による表面処理装置は、横断面形状が楕円形や多角形の棒状の陽電極部材又は陰電極部材の他方を備えていてもよい。
4.本発明による表面処理装置は、単一の棒状の陽電極部材又は陰電極部材の他方を備えていてもよい。
5.本発明による表面処理装置は、棒状の陽電極部材又は陰電極部材の他方を、その長手方向が被処理物の外周面に対して斜めの方向となるように突設してあってもよい。
6.本発明による表面処理装置は、棒状の陽電極部材又は陰電極部材の他方を、その長手方向が電解液通路における電解液の流れ方向上手側に向かう斜めの方向となるように突設してあっても、流れ方向下手側に向かう斜めの方向となるように突設してあってもよい。
7.本発明による表面処理装置は、表面処理としての電気メッキ処理を行うための電気メッキ処理装置であってもよい。
[Other Embodiments]
1. The surface treatment apparatus according to the present invention may perform a surface treatment on a convex surface (mountain shape) or a planar annular region to be processed which is provided on the outer peripheral surface of an object to be processed.
2. The surface treatment apparatus according to the present invention includes a negative electrode member that is electrically connected to a metal object to be processed, and a protrusion that projects toward the object to be processed so that the tip portion enters the electrolyte passage. A certain rod-shaped positive electrode member may be provided.
3. The surface treatment apparatus according to the present invention may include the other of a positive electrode member or a negative electrode member in the shape of an ellipse or polygonal bar.
4). The surface treatment apparatus according to the present invention may include the other of a single rod-like positive electrode member or negative electrode member.
5. In the surface treatment apparatus according to the present invention, the other of the rod-shaped positive electrode member or the negative electrode member may be provided so that the longitudinal direction thereof is an oblique direction with respect to the outer peripheral surface of the workpiece.
6). In the surface treatment apparatus according to the present invention, the other of the rod-like positive electrode member or the negative electrode member is projected so that the longitudinal direction thereof is an oblique direction toward the upper side of the electrolyte flow direction in the electrolyte passage. Alternatively, it may be provided so as to project in an oblique direction toward the lower side in the flow direction.
7). The surface treatment apparatus according to the present invention may be an electroplating apparatus for performing an electroplating process as a surface treatment.

2 電解液通流手段
15 陽電極部材又は陰電極部材の一方(陽電極部材)
17 枠部材
26 周溝
31 非導電性の内周面
36 電解液供給ノズル
38 電解液排出流路
40 弾性シール材
41 棒状の陽電極部材又は陰電極部材の他方(陰電極部材)
45 電解液通路
46a 先端部
57 凹凸面
A 被処理物
A1 環状被処理領域(周溝)
B 外周面
C 隙間
2 Electrolyte flow means 15 One of positive electrode member or negative electrode member (positive electrode member)
17 Frame member 26 Circumferential groove 31 Non-conductive inner peripheral surface 36 Electrolyte supply nozzle 38 Electrolyte discharge channel 40 Elastic seal material 41 The other of the rod-shaped positive electrode member or negative electrode member (negative electrode member)
45 Electrolyte passage 46a Tip portion 57 Uneven surface A Object A1 Annular region (circumferential groove)
B Outer peripheral surface C Clearance

Claims (6)

環状被処理領域を外周面の円周方向に沿って有する円柱状の金属製の被処理物に電気的に接続される陽電極部材又は陰電極部材の一方と、
前記外周面及び前記環状被処理領域に対して間隔を隔てて対向する非導電性の内周面を備えた枠部材と、
前記外周面のうち前記環状被処理領域を挟んだ両側夫々と前記内周面との隙間をシールすることにより、前記環状被処理領域に沿った電解液通路を形成可能な非導電性の弾性シール材と、
先端部が前記電解液通路の中に入り込むように前記被処理物の側に向けて突設してある棒状の陽電極部材又は陰電極部材の他方と、
前記電解液通路に沿って電解液を通流させる電解液通流手段とを備えている表面処理装置。
One of a positive electrode member or a negative electrode member electrically connected to a cylindrical metal object to be processed having an annular treatment area along the circumferential direction of the outer peripheral surface;
A frame member having a non-conductive inner peripheral surface facing the outer peripheral surface and the annular processing region with a gap therebetween;
A non-conductive elastic seal capable of forming an electrolyte passage along the annular processing region by sealing a gap between each of the outer peripheral surfaces sandwiching the annular processing region and the inner peripheral surface. Material,
The other of the rod-shaped positive electrode member or negative electrode member protruding toward the object to be processed so that the tip portion enters the electrolyte passage,
A surface treatment apparatus comprising: an electrolyte solution flow means for causing the electrolyte solution to flow along the electrolyte solution passage.
前記環状被処理領域に向けて開口する複数の電解液供給ノズルと、
前記枠部材の前記内周面に一定の溝幅で形成された周溝とを備え、
前記電解液供給ノズルの夫々が、前記周溝の溝内に溝周方向に互いに間隔を隔てて配設され、
前記周溝のうちの、隣り合う電解液供給ノズルどうしの間の周溝部分が、電解液排出流路として形成され、
前記隣り合う電解液供給ノズルどうしの間隔を、ノズル先端箇所において最も狭くなるように設定してある請求項1記載の表面処理装置。
A plurality of electrolyte supply nozzles opening toward the annular processing region;
A circumferential groove formed with a constant groove width on the inner circumferential surface of the frame member,
Each of the electrolyte solution supply nozzles is disposed in the circumferential groove at a distance from each other in the circumferential direction of the groove,
Of the circumferential groove, a circumferential groove portion between adjacent electrolyte supply nozzles is formed as an electrolyte discharge flow path,
The surface treatment apparatus according to claim 1, wherein an interval between the adjacent electrolyte supply nozzles is set to be narrowest at a nozzle tip portion.
前記棒状の陽電極部材又は陰電極部材の他方の複数を前記電解液通路の周方向に沿って分散配置してある請求項1又は2記載の表面処理装置。   The surface treatment apparatus according to claim 1 or 2, wherein a plurality of the other of the rod-shaped positive electrode members or negative electrode members are dispersedly arranged along the circumferential direction of the electrolyte passage. 前記棒状の陽電極部材又は陰電極部材の他方を、その長手方向が前記外周面に対して直交する方向となるように突設してある請求項1〜3のいずれか1項記載の表面処理装置。   The surface treatment according to any one of claims 1 to 3, wherein the other of the rod-shaped positive electrode member or the negative electrode member is projected so that the longitudinal direction thereof is perpendicular to the outer peripheral surface. apparatus. 前記棒状の陽電極部材又は陰電極部材の他方の外周面を凹凸面に形成してある請求項1〜4のいずれか1項記載の表面処理装置。   The surface treatment apparatus of any one of Claims 1-4 which has formed the other outer peripheral surface of the said rod-shaped positive electrode member or negative electrode member in an uneven surface. 前記棒状の陽電極部材又は陰電極部材の他方における先端部の形状を凸曲面状に形成してある請求項1〜5のいずれか1項記載の表面処理装置。   The surface treatment apparatus according to any one of claims 1 to 5, wherein a shape of a tip portion of the other of the rod-shaped positive electrode member and the negative electrode member is formed in a convex curved surface shape.
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JP2012007234A (en) 2012-01-12

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