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JP4677829B2 - Anodizing equipment for metal parts - Google Patents

Anodizing equipment for metal parts Download PDF

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JP4677829B2
JP4677829B2 JP2005159849A JP2005159849A JP4677829B2 JP 4677829 B2 JP4677829 B2 JP 4677829B2 JP 2005159849 A JP2005159849 A JP 2005159849A JP 2005159849 A JP2005159849 A JP 2005159849A JP 4677829 B2 JP4677829 B2 JP 4677829B2
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electrode
electrolytic solution
electrolyte
anodizing apparatus
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JP2006336050A (en
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敏也 小島
岳世 和田
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Aisin Corp
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Aisin Seiki Co Ltd
Aisin Corp
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Description

本発明は、表面にリング状の凹部を持つ金属製部品の陽極酸化処理装置に関するものである。   The present invention relates to an anodizing apparatus for metal parts having a ring-shaped recess on the surface.

一般的に陽極酸化処理は、硫酸、クロム酸などを含む酸性電解液を用いて被処理物を正極側にし、通電することにより、例えばアルミニウム基金属製被処理物の表面を酸化し、アルマイト膜厚を形成する処理方法である。しかしアルマイト膜厚が増加すると、その被膜特性(絶縁性)から、電気が流れにくくなり、酸化効果が低下する。このため必要とする膜厚を達成するには、長時間を必要とし、生産効率が悪い。   In general, anodic oxidation is performed by using an acidic electrolytic solution containing sulfuric acid, chromic acid or the like to bring the object to be treated to the positive electrode side and energizing, for example, to oxidize the surface of the aluminum-based metal object to be treated. It is the processing method which forms thickness. However, when the alumite film thickness increases, electricity becomes difficult to flow due to its film characteristics (insulating properties), and the oxidation effect decreases. Therefore, it takes a long time to achieve the required film thickness, and the production efficiency is poor.

効率よく所定厚さのアルマイト膜を得るために、流れる電流密度を向上させ、大電流により陽極酸化処理することにより時間を短縮することができるが、多量のジュール熱が発生する。また、近年、材料強度アップのために、多量のシリコンを含むアルミニウム合金が使用されている。このようなアルミニウム合金ではさらに多くの発熱がある。よって、効率よく発生した熱を除去しなければ被膜の硬度の低下が発生し、バーニング現象として現れる。従って、膜厚を増大させるに伴い、アルマイト被膜層への冷却が必要となる。   In order to efficiently obtain an alumite film having a predetermined thickness, the current density can be improved and the time can be shortened by anodizing with a large current, but a large amount of Joule heat is generated. In recent years, aluminum alloys containing a large amount of silicon have been used to increase material strength. Such an aluminum alloy generates more heat. Therefore, if the generated heat is not removed efficiently, the hardness of the coating is lowered, and appears as a burning phenomenon. Accordingly, as the film thickness is increased, cooling to the alumite coating layer is required.

バーニング現象を防止し、被膜層を冷却する方法としては、特開平11−236696号公報において、電解液浴中で多数の電解液噴射口より電解液を流速30cm/sec〜300cm/secで被処理物に当てて、アルマイト被膜を形成する方法が開示されている。この方法では、4.8μm/分のアルマイト膜形成速度が得られるが、浴中での電解液噴出には大出力のポンプが必要となり、設備投資によるコストアップとなる。また、特開平4−198497号公報に記載の方法では、アルマイト膜形成速度は12.9μm/分が得られる。さらに、この方法では、アルミニウム合金製のピストン頂部などの表面にアルマイト被膜の形成は可能である。しかし、ピストンリング溝等の、溝部への被膜形成はできない。   As a method for preventing the burning phenomenon and cooling the coating layer, in Japanese Patent Application Laid-Open No. 11-236696, the electrolytic solution is treated at a flow rate of 30 cm / sec to 300 cm / sec in an electrolytic bath from a number of electrolytic solution injection ports. A method of forming an alumite coating on an object is disclosed. In this method, an alumite film formation rate of 4.8 μm / min can be obtained, but a high-power pump is required for spraying the electrolyte in the bath, which increases costs due to capital investment. Further, according to the method described in JP-A-4-198497, an alumite film formation rate of 12.9 μm / min is obtained. Furthermore, in this method, an alumite film can be formed on the surface of an aluminum alloy piston top or the like. However, it is not possible to form a coating on the groove portion such as the piston ring groove.

さらに、特開平9−217200号公報は、頂面に対向した位置に回転噴射盤を設置し、被処理面にアルマイト被膜層生成時の発熱に対する冷却を向上させている。アルマイト膜形成速度は15.0μm/分である。   Further, Japanese Patent Laid-Open No. 9-217200 provides a rotating spray disc at a position facing the top surface to improve cooling against heat generated when the alumite coating layer is formed on the surface to be processed. The alumite film formation rate is 15.0 μm / min.

いずれの場合もアルミニウム基金属製部品の被処理物の外側、すなわち、平面部、凸部への処理方法及び装置を開示しているが、凹部(溝部)への高速処理は実現できていない。
特開平11−236696号公報 特開平9−217200号公報 特開平4−198497号公報
In either case, a processing method and apparatus for the outside of the workpiece of an aluminum-based metal part, that is, a flat surface portion and a convex portion are disclosed, but high-speed processing to a concave portion (groove portion) cannot be realized.
JP-A-11-236696 JP 9-217200 A JP-A-4-198497

本発明の目的は、上記の点に鑑み、凹部表面をもつ金属製部品の凹部に金属酸化被膜を形成する表面陽極酸化処理装置を提供することにある。   An object of the present invention is to provide a surface anodizing apparatus for forming a metal oxide film in a concave portion of a metal part having a concave surface in view of the above points.

課題を解決するための手段、作用、効果Means, actions, and effects to solve the problem

本発明の金属製部品の陽極酸化処理装置は、側周面の被処理面にリング状の凹部を持つ筒状の被処理物に電流を通電する第1電極部と、該第1電極部との間に電圧が印加される電極本体を有する第2電極部と、前記第2電極部を通して電解液を供給する電解液供給手段と、前記第1電極部と前記第2電極部との間前記電圧を印加する通電手段と、備える陽極酸化処理装置において、前記電極本体は、前記被処理面を囲むように対向する内周面、及び該内周面を周壁とし上面が開口した液槽を有し、該内周面には、前記凹部に対向し該凹部に向かって電解液を噴射する複数の吐出孔を有することを特徴とする。 An apparatus for anodizing a metal part according to the present invention includes a first electrode portion for energizing a cylindrical object to be processed having a ring-shaped recess on a surface to be processed on the side peripheral surface, the first electrode portion, a second electrode portion having an electrode body when a voltage is applied between the, and the electrolytic solution supply means that teapot subjected electrolyte through the second electrode portion, and the first electrode portion and the second electrode portion energizing means for applying the voltage between, the anodic oxidation processing apparatus including the electrode body, the inner peripheral surface opposed to surround the treated surface, and the upper surface and the inner peripheral surface and the peripheral wall is opened the liquid A tank is provided, and the inner peripheral surface has a plurality of discharge holes that oppose the recess and inject an electrolyte toward the recess .

本発明の表面陽極酸化処理装置では、内側に吐出穴を持つ第2電極部を持ち、その吐出穴は被処理物の凹部に対向している。そして電解液供給手段で電解液を第2電極部の吐出孔より噴出させ、同時に通電手段により保持手段を介して被処理物を第1電極(陽極)とし第2電極(陰極)との間に電圧を印加する。吐出孔より噴出する電解液は被処理物の凹部を満たし通電により第2電極部に対向する被処理物の凹部は優先的に陽極酸化され金属酸化被膜が形成される。凹部内の電解液は通電により発生する熱により加熱されて温度が上昇するが、凹部を満たす電解液は吐出孔より噴出する電解液で常に新しい冷たい電解液が供給され、凹部の温度上昇は限られた低いものとなる。これによりバーニング現象等の不都合を伴うことなく、被処理物の凹部を効率よく陽極酸化処理でき、被処理物の凹部表面に短時間に厚い金属酸化被膜を形成することができる。   The surface anodizing apparatus of the present invention has a second electrode portion having a discharge hole on the inside, and the discharge hole faces the concave portion of the object to be processed. Then, the electrolytic solution is ejected from the discharge hole of the second electrode portion by the electrolytic solution supply means, and at the same time, the object to be processed is made the first electrode (anode) through the holding means by the energizing means, and between the second electrode (cathode). Apply voltage. The electrolytic solution ejected from the discharge hole fills the concave portion of the workpiece, and the concave portion of the workpiece facing the second electrode portion is preferentially anodized by energization to form a metal oxide film. The electrolyte in the recess is heated by the heat generated by energization and the temperature rises, but the electrolyte that fills the recess is always supplied with a new, cold electrolyte from the discharge hole, and the rise in temperature of the recess is limited. Will be low. Accordingly, the concave portion of the object to be processed can be efficiently anodized without inconvenience such as a burning phenomenon, and a thick metal oxide film can be formed on the concave surface of the object to be processed in a short time.

本発明の金属製部品の陽極酸化処理装置は、第1電極部と、第2電極部と、電解液供給手段と、通電手段とを有する。   The anodizing apparatus for metal parts of the present invention includes a first electrode part, a second electrode part, an electrolyte supply means, and an energization means.

第1電極部は、被処理物に接触する導電体で構成される。   A 1st electrode part is comprised with the conductor which contacts a to-be-processed object.

導電体としては通電性を必要とするため、通電性のよい金属製材料が好ましい。   Since the conductive material requires electrical conductivity, a metal material with good electrical conductivity is preferable.

被処理物としては、金属製で表面にリング状の凹部を持つものである。具体的にアルミニウム合金製のピストンを例示することができる。ピストンのように筒状、棒状でその外表面に外周を一周するリング溝を持つものが好ましい。ここでアルミニウム基金属とは、アルミニウム金属及びアルミニウムに銅、亜鉛、ケイ素等の他の元素を混合した合金をも含む。   The object to be processed is made of metal and has a ring-shaped recess on the surface. Specifically, an aluminum alloy piston can be exemplified. It is preferable to use a cylindrical or rod-like ring groove having a ring groove that goes around the outer periphery on its outer surface. Here, the aluminum-based metal includes an aluminum metal and an alloy obtained by mixing other elements such as copper, zinc, and silicon with aluminum.

また、第1電極部は被処理物を保持する保持手段に組み込まれたものとすることができる。また、保持手段は保持する被処理物を回転駆動させる回転手段としての回転駆動部を持つことができる。回転駆動部は、被処理物が該被処理物の軸を中心として回転するものとすることができる。また、保持手段は被処理物を、例えば着脱位置と電解処理位置に移動させる移動手段を持つものとすることができる。   Further, the first electrode part can be incorporated in a holding means for holding the object to be processed. Further, the holding means can have a rotation driving unit as a rotating means for rotating the workpiece to be held. The rotation driving unit may be configured such that the object to be processed rotates around the axis of the object to be processed. Further, the holding means may have a moving means for moving the object to be processed to, for example, an attachment / detachment position and an electrolytic treatment position.

第2電極部は、電解液通路を備え、被処理物の側周面を囲う内周面を有し、該内周面に電解液通路に連通し、被処理物の凹部に対向する吐出孔を有するものである。   The second electrode portion includes an electrolyte passage, has an inner peripheral surface surrounding a side peripheral surface of the object to be processed, and communicates with the electrolyte passage on the inner peripheral surface and discharge holes facing the concave portion of the object to be processed. It is what has.

内周面の形状および吐出孔の形状は被処理物の被処理面に合わせ、異なる形状を持つことができる。凹部を持つ被処理面に合わせた吐出孔の形状は円形が一般的であるが、場合によって、楕円形、あるいは方形も好ましい。また、吐出孔は第2電極部の内側に1個又は複数個リングの延びる方向に離間して配列することもできる。第2電極部の吐出孔の数、吐出孔のサイズ等も被処理物に合わせて自由に設定することができる。   The shape of the inner peripheral surface and the shape of the discharge hole can have different shapes according to the surface to be processed of the object to be processed. The shape of the discharge hole matched to the surface to be processed having a recess is generally circular, but in some cases, an elliptical shape or a rectangular shape is also preferable. Further, the discharge holes may be arranged inside the second electrode portion so as to be separated from each other in the extending direction of one or a plurality of rings. The number of discharge holes of the second electrode part, the size of the discharge holes, and the like can be freely set according to the object to be processed.

アルミニウム合金製ピストンを被処理物とした場合、吐出孔径は0.5〜2.0mmで、吐出孔数は4〜32個が好ましい。また、第2電極部は通電性を必要とするため、通電性のよい金属製材料が好ましい。   When an aluminum alloy piston is used as the workpiece, the discharge hole diameter is preferably 0.5 to 2.0 mm and the number of discharge holes is preferably 4 to 32. In addition, since the second electrode portion requires electrical conductivity, a metal material with good electrical conductivity is preferable.

電解液供給手段は、電解液を貯留する貯留槽と、該貯留槽と電解液通路とを接続する流入路と、流入路に配置され貯留槽から電解液通路に電解液を送出するポンプとで構成することができる。   The electrolytic solution supply means includes a storage tank that stores the electrolytic solution, an inflow path that connects the storage tank and the electrolytic solution passage, and a pump that is disposed in the inflow path and sends the electrolytic solution from the storage tank to the electrolytic solution passage. Can be configured.

また、電解液供給手段には電解液を冷却させる冷却手段、及び電解液の温度を制御する温度制御手段、電解液の流量を制御する流量制御手段を設けることもできる。   The electrolyte supply means may be provided with a cooling means for cooling the electrolyte, a temperature control means for controlling the temperature of the electrolyte, and a flow rate control means for controlling the flow rate of the electrolyte.

また、第2電極部は電解液を収集する貯留槽を組んで構成することが好ましい。貯留槽は被処理物に噴射された後の電解液を収集し、供給手段に送出する。貯留槽本体は上端開放の容器状のものでも、被処理物によっては密閉された容器状のものでも良い。貯留槽は一個、あるいは複数個で連通設置することができる。電解液は強酸を用いる場合が多いことから、貯留槽本体の材質はSUS316あるいは塩化ビニル製が好ましい。貯留槽が第2電極部とは、一体的に構成されていても着脱自在に形成されていてもよい。   Moreover, it is preferable that the 2nd electrode part is comprised combining the storage tank which collects electrolyte solution. The storage tank collects the electrolytic solution after being sprayed on the object to be processed and sends it out to the supply means. The storage tank main body may be a container with an open top or a sealed container depending on the object to be processed. One or a plurality of storage tanks can be installed in communication. Since the electrolytic solution often uses strong acid, the material of the storage tank body is preferably SUS316 or vinyl chloride. The storage tank may be formed integrally with the second electrode portion or may be detachable.

通電手段は、第1電極部と第2陰極部との間に電圧を印加する手段である。この通電手段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、従来公知のものを用いることができる。   The energization means is means for applying a voltage between the first electrode portion and the second cathode portion. This energization means preferably has current control means so that the current density can be adjusted. The current control means includes an ammeter, a voltmeter, a rectifier and the like, and a conventionally known one can be used.

以下、実施例に基づいて本発明の陽極酸化処理装置を詳細に説明する。本実施例の陽極酸化処理装置の機能説明図を図1に示す。この陽極酸化処理装置はアルミニウム合金製のピストンWのピストンリング溝W1を陽極酸化処理するものである。より正確にはピストンWの頂部の外周面にある頂部より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W1、W2及びW3の内、頂部側のピストンリング溝W1を含む頂部外周面を主として陽極酸化処理するものである。   Hereinafter, based on an Example, the anodizing apparatus of this invention is demonstrated in detail. A functional explanatory diagram of the anodizing apparatus of this embodiment is shown in FIG. This anodizing apparatus is for anodizing a piston ring groove W1 of a piston W made of aluminum alloy. More precisely, of the three piston ring grooves W1, W2 and W3 formed from the top to the skirt on the outer peripheral surface of the top of the piston W, the top outer peripheral surface including the piston ring groove W1 on the top side is mainly used as the anode. It is an oxidation treatment.

この陽極酸化処理装置は、ピストンWを保持する保持手段1と、リング状電極を構成する電極部2を持つ電解槽3と、電解液供給手段4と、通電手段5とを有する。   This anodizing apparatus has a holding means 1 for holding a piston W, an electrolytic cell 3 having an electrode portion 2 constituting a ring-shaped electrode, an electrolyte supply means 4, and an energizing means 5.

保持手段1はフレーム(図示せず)の上端に固定された昇降装置(図示せず)の昇降部に固定された減速モータ11とこの減速モータ11の出力軸に固定された保持軸12とからなる。保持軸12の下端にはピストンWの内周面に着脱自在の係止爪(図示せず)が設けられている。この係止爪にはその下端側からピストンWの内腔が覆い被さるように軸方向に挿入され、保持軸12とピストンWは同軸的となる。なお、保持軸12の軸方向中程に、後で説明する、通電手段5を構成する集電リング51が固定され、この集電リング51と図示しない係止爪とは電気的に電通し、かつ係止爪を介してピストンWに電通している。なお、集電リング51及び保持軸12は本発明の第1電極部を構成するものである。   The holding means 1 includes a reduction motor 11 fixed to an elevating part of an elevating device (not shown) fixed to an upper end of a frame (not shown), and a holding shaft 12 fixed to an output shaft of the reduction motor 11. Become. A detachable locking claw (not shown) is provided on the inner peripheral surface of the piston W at the lower end of the holding shaft 12. The locking claw is inserted in the axial direction so as to cover the inner cavity of the piston W from the lower end side, and the holding shaft 12 and the piston W are coaxial. In addition, a current collecting ring 51 constituting the energizing means 5 described later is fixed in the middle of the holding shaft 12 in the axial direction, and the current collecting ring 51 and an engaging claw (not shown) are electrically connected. And it is electrically connected to the piston W through the locking claw. The current collecting ring 51 and the holding shaft 12 constitute the first electrode portion of the present invention.

また、ピストンWの頂部を除くピストンリング溝W2とピストンリング溝W3の境界を形成する突条の外周面には筒状のゴム製マスキングW5が装着固定され、ピストンWの頂部を除く下方部は電解液が接触しないようにカバーされている。また、集電リング51と、保持軸12と、ピストンWとにより陽極が構成される。   A cylindrical rubber masking W5 is mounted and fixed on the outer peripheral surface of the ridge forming the boundary between the piston ring groove W2 and the piston ring groove W3 excluding the top of the piston W, and the lower part excluding the top of the piston W is Covered so that the electrolyte does not touch. The current collecting ring 51, the holding shaft 12, and the piston W constitute an anode.

電極部2は、その拡大縦断面図及び平面図をそれぞれ図2、図3に示すように、方形状の基板21と円盤状の中板22とリング状の電極本体23と導体24とから構成されている。なお、電極部2は本発明の第2電極部(陰極)を構成するものである。   The electrode section 2 is composed of a rectangular substrate 21, a disk-shaped intermediate plate 22, a ring-shaped electrode body 23, and a conductor 24, as shown in FIGS. Has been. In addition, the electrode part 2 comprises the 2nd electrode part (cathode) of this invention.

基板21はSUS316製で、その縦断面図及び平面図をそれぞれ図4及び図5に示すように、四隅が丸く形成された方形の板状で、その上面に浅い円形の凹部211とその凹部の中央に一端が開口し他端が側面に開口するトンネル状の通路212を持つ。   The substrate 21 is made of SUS316, and as shown in FIG. 4 and FIG. 5 in the longitudinal sectional view and the plan view, respectively, is a square plate shape with rounded four corners. A tunnel-like passage 212 having one end opened at the center and the other end opened on the side surface is provided.

中板22は塩化ビニル製で、その縦断面図及び平面図をそれぞれ図6及び図7に示すように、円盤状でその下面側には中央部に浅い円形凹部221を形成する突条222と、上面側の中央部に深い円形溝223とこれと同軸の浅い円形溝224を形成する段付き突条225を持つ。さらに下面側の円形凹部221と上面側の浅い円形溝224とに両端が開口する通孔226が形成されている。この通孔226は等間隔のリング状に8個設けられている。さらにこの中板22には、その外周面から深い円形溝223に表出する導体24が組み込まれている。   The middle plate 22 is made of vinyl chloride, and its longitudinal sectional view and plan view are shown in FIGS. 6 and 7, respectively. As shown in FIGS. And a stepped ridge 225 for forming a deep circular groove 223 and a shallow circular groove 224 coaxial with the deep circular groove 223 at the center on the upper surface side. Further, through holes 226 having both ends opened are formed in the circular recess 221 on the lower surface side and the shallow circular groove 224 on the upper surface side. Eight of the through holes 226 are provided in a ring shape with equal intervals. Further, the intermediate plate 22 incorporates a conductor 24 that is exposed from the outer peripheral surface thereof to the deep circular groove 223.

電極本体23はSUS316製で、その縦断面図及び平面図をそれぞれ図8及び図9に示すように、外周部が二段となる段付き円筒状である。リング状の下面231に開口する8個の流入口と内周面232に軸方向に2段となる1段8個で2段で合計16個の吐出孔をもつ8個の通孔233が形成されている。これら通孔233は前記中板22に設けられた8個の通孔226と同位置にあり、中板22の通孔226と電極本体23の通孔233は連通するようになり、電解液通路となる。なお、通孔233の内周面232側の開口は電解液の吐出孔となり、いずれも電極本体23の軸心に向かって開口している。このため電解液は水平方向に軸心に向かって吐出する。また、中板22に導体24が設けられるため、電極本体23は中板22と嵌合する際、導体24を介して電通する。   The electrode body 23 is made of SUS316, and has a stepped cylindrical shape with two outer peripheral portions as shown in FIGS. Eight inflow holes 233 having a total of 16 discharge holes in two stages are formed on the inner peripheral surface 232 with eight inflow openings that open in the ring-shaped lower surface 231 and two stages in the axial direction. Has been. These through holes 233 are located at the same positions as the eight through holes 226 provided in the intermediate plate 22, and the through holes 226 of the intermediate plate 22 and the through holes 233 of the electrode body 23 communicate with each other, so that the electrolyte passage It becomes. Note that the opening on the inner peripheral surface 232 side of the through hole 233 serves as an electrolyte discharge hole, and both are open toward the axis of the electrode body 23. For this reason, electrolyte solution is discharged toward an axial center in a horizontal direction. In addition, since the conductor 24 is provided on the intermediate plate 22, the electrode body 23 is electrically connected via the conductor 24 when fitted to the intermediate plate 22.

電極部2を有する電解槽3は、塩化ビニル製又はSUS316製で、上端開口する容器状ものであり、さらに電解槽3の底に受け溜まった電解液を供給手段4に回収させる回収口31が設けられている。なお、電解槽3は本発明の貯留槽の一部を構成するものである。   The electrolytic cell 3 having the electrode part 2 is made of vinyl chloride or SUS316, is a container having an opening at the upper end, and further has a collection port 31 for collecting the electrolytic solution collected at the bottom of the electrolytic cell 3 to the supply means 4. Is provided. In addition, the electrolytic cell 3 comprises a part of storage tank of this invention.

電解液供給手段4は、電解槽3から回収された電解液を冷却させる冷却槽41と、電解液を送出す駆動手段であるポンプ43と、電解液の流量を制御する流量制御手段である流量計44と、ポンプ43から圧送される電解液を送るパイプ45とから構成されている。さらに、冷却槽41には、電解液を貯蔵するサブタンク411と、回収された電解液を冷却させる手段である冷凍機412と、電解液の温度を制御する制御手段を構成する温度センサ413が設けられている。なお、パイプ45は本発明の流入路を構成するものである。冷却槽41は本発明の貯留槽の一部を構成するものである。   The electrolyte supply means 4 is a cooling tank 41 that cools the electrolyte recovered from the electrolytic tank 3, a pump 43 that is a drive means that sends out the electrolyte, and a flow rate that is a flow rate control means that controls the flow rate of the electrolyte. It is composed of a total 44 and a pipe 45 for feeding an electrolyte solution pumped from the pump 43. Further, the cooling tank 41 is provided with a sub-tank 411 for storing the electrolyte, a refrigerator 412 that is a means for cooling the recovered electrolyte, and a temperature sensor 413 that constitutes a control means for controlling the temperature of the electrolyte. It has been. The pipe 45 constitutes the inflow path of the present invention. The cooling tank 41 constitutes a part of the storage tank of the present invention.

通電手段5は、電極本体23と保持手段1で保持されるピストンWとの間に電圧を印加する手段であり、電流計、電圧計、整流器(図示せず)等で構成されている。   The energizing means 5 is means for applying a voltage between the electrode body 23 and the piston W held by the holding means 1 and is composed of an ammeter, a voltmeter, a rectifier (not shown), and the like.

また、本実施例では、電極本体23の吐出孔234による電解液が噴射される際、吐出孔234の形状及びサイズは陽極酸化処理の効果に影響することから、円形として形成されたが、実際に陽極酸化処理が行われる際、場合によっては吐出孔234を楕円形、または方形形状にすることも可能である。さらに、電極本体23の吐出孔234の均等性が保証される限り、吐出孔234は電極本体23の内周面に複数組の段列配置ができる。   Further, in this embodiment, when the electrolyte solution is ejected from the discharge hole 234 of the electrode body 23, the shape and size of the discharge hole 234 affects the effect of the anodizing treatment. When the anodizing process is performed, the discharge hole 234 may be elliptical or rectangular in some cases. Furthermore, as long as the uniformity of the discharge holes 234 of the electrode body 23 is ensured, the discharge holes 234 can be arranged in a plurality of sets on the inner peripheral surface of the electrode body 23.

また、実施例では、電解液を吐出孔234から被処理物であるピストンWの頂部側のピストンリング溝W1を含む頂部外周面の表面に噴射される際、電極本体23の内周面232と被処理面を構成するピストンリング溝W1との間の距離は陽極酸化処理の効果に影響する。被処理面が陰極となる電極本体23の内周面232に近すぎるとショ−トする可能性が生じる。逆に、被処理面と電極本体23の内周面232間の距離は離れすぎると電解液が有効的に該被処理面まで到達されず、陽極酸化処理が不十分となる。従って、陽極に接続されているピストンWの頂部側の2本のピストンリング溝W1を含む頂部外周面の表面から電極本体23の吐出孔234間の距離が2.0〜15.0mmであることが好ましい。   Further, in the embodiment, when the electrolytic solution is sprayed from the discharge hole 234 to the surface of the top outer peripheral surface including the piston ring groove W1 on the top side of the piston W that is the object to be processed, the inner peripheral surface 232 of the electrode body 23 The distance from the piston ring groove W1 constituting the surface to be processed affects the effect of the anodizing process. If the surface to be processed is too close to the inner peripheral surface 232 of the electrode main body 23 to be the cathode, there is a possibility that a short will occur. On the other hand, if the distance between the surface to be processed and the inner peripheral surface 232 of the electrode body 23 is too large, the electrolytic solution does not effectively reach the surface to be processed, and the anodizing treatment becomes insufficient. Therefore, the distance between the discharge hole 234 of the electrode main body 23 from the surface of the top outer peripheral surface including the two piston ring grooves W1 on the top side of the piston W connected to the anode is 2.0 to 15.0 mm. Is preferred.

さらに、電解液が噴射される際、吐出孔234に面する箇所が強く噴射噴流され、形成されたアルマイト被膜は不均一である問題に対して、ピストンWを保持する保持手段1を回転させる回転手段として減速モーター11が装備されているため、ピストンWを回転しながら電解液を噴射させることによってアルマイト被膜を均一に形成することができる。   Further, when the electrolyte solution is injected, the portion facing the discharge hole 234 is strongly injected and jetted, and the rotation of the holding means 1 for holding the piston W is rotated for the problem that the formed alumite film is not uniform. Since the decelerating motor 11 is provided as a means, the alumite film can be uniformly formed by injecting the electrolyte while rotating the piston W.

次にアルミニウム基金属製部品を陽極酸化処理する際の電解液の経路を説明する。供給手段4に組み込まれている冷却槽41で冷却された電解液は、流量制御手段44により流量が制御され、循環ポンプ43により、電解槽3に送られる。電解液は電解槽3にある基板21のトンネル状通路212から、基板21の上面側凹部211と中板22の下面側凹部221間からなるチャンバーを昇り、中板22の通孔226と電極本体23の通孔233からなる電解液通路を通過し、吐出孔234からピストンリング溝W1を含む頂部外周面に噴射される。さらに、電解液が吐出孔234から噴射され、陽極酸化処理が行われた後、電極本体23と中板22から構成される小容器の液槽に溜まると共に、上方にオーバーブローしていく。オーバーフローした電解液は、電極部2の外側を通り、電解槽3の底の回収穴31を通じて、供給手段4に回収される。供給手段4が保有する冷却手段412により冷却され、再び電解槽3に送られる。   Next, the route of the electrolytic solution when anodizing the aluminum-based metal part will be described. The flow rate of the electrolytic solution cooled in the cooling tank 41 incorporated in the supply unit 4 is controlled by the flow rate control unit 44 and sent to the electrolytic cell 3 by the circulation pump 43. The electrolyte rises from the tunnel-shaped passage 212 of the substrate 21 in the electrolytic cell 3 to the chamber formed between the upper surface side recess 211 of the substrate 21 and the lower surface side recess 221 of the intermediate plate 22, and the through hole 226 of the intermediate plate 22 and the electrode body 23 passes through the electrolyte passage made up of 23 through-holes 233 and is sprayed from the discharge holes 234 to the top outer peripheral surface including the piston ring groove W1. Furthermore, after the electrolytic solution is sprayed from the discharge hole 234 and anodized, it accumulates in a liquid container of a small container composed of the electrode body 23 and the middle plate 22 and overblows upward. The overflowing electrolyte solution passes through the outside of the electrode unit 2 and is collected by the supply means 4 through the collection hole 31 at the bottom of the electrolytic cell 3. It is cooled by the cooling means 412 held by the supply means 4 and sent to the electrolytic cell 3 again.

以下、本発明の実施例に基づいてアルマイト処理を行った結果を説明する。図1に示したように、電解槽3には、アルミニウム基金属製ピストンWを保持手段1に固定させ、集電リング51を介して陽極に接続する。電極部2は口径が1.5mmで1段8個の吐出孔234が設けられ、2段列で配列され、陽極と共に電気回路を構成する。アルミニウム基金属製ピストンWの溝部表面から電極本体23の内周面232間の距離は2.5mmである。   Hereinafter, the results of performing anodizing based on the examples of the present invention will be described. As shown in FIG. 1, in the electrolytic cell 3, an aluminum base metal piston W is fixed to the holding means 1 and connected to the anode via a current collecting ring 51. The electrode part 2 has a diameter of 1.5 mm, is provided with eight discharge holes 234 in one stage, is arranged in two stages, and constitutes an electric circuit together with the anode. The distance between the groove surface of the aluminum base metal piston W and the inner peripheral surface 232 of the electrode body 23 is 2.5 mm.

表1は、各試験における、電流密度、処理電圧、回転数、電解液濃度、電解液温度、アルマイト処理速度及びアルマイト膜厚のデータを示す。   Table 1 shows data on current density, processing voltage, rotation speed, electrolytic solution concentration, electrolytic solution temperature, alumite treatment speed, and alumite film thickness in each test.

Figure 0004677829
Figure 0004677829

なお、比較例は、従来の方法で電解液に被処理物であるピストンの先端部のみを漬けて電解処理を行ったものである。   In the comparative example, the electrolytic treatment was performed by immersing only the tip portion of the piston as the object to be treated in the electrolytic solution by the conventional method.

表1により、本発明の装置によるアルミニウム基金属製ピストンのピストンリング溝部の陽極酸化処理を行った結果、本発明の実施例の陽極酸化処理装置ではアルマイト処理速度として25μm/分という早い速度で健全なアルマイト被膜が形成できることが明らかになった。従来の装置ではアルマイト処理速度が1.3μm/分であり、本発明の陽極酸化処理装置では従来装置の約20倍の被膜形成速度を持つ。被膜形成速度が極めて速いにも関わらずバーニング等の悪い現象が起こらないのは吐出孔より電解液を噴出し常に冷却された電解液が被処理面に供給され、被処理物が効率良く冷却されるためと考えられる。   According to Table 1, as a result of anodizing the piston ring groove portion of the aluminum-based metal piston by the apparatus of the present invention, the anodizing apparatus of the embodiment of the present invention is healthy at a speed as fast as 25 μm / min. It became clear that an alumite film can be formed. The conventional apparatus has an alumite treatment speed of 1.3 μm / min, and the anodizing apparatus of the present invention has a film formation speed about 20 times that of the conventional apparatus. Even though the film formation speed is extremely high, the phenomenon of burning and the like does not occur. The electrolytic solution is ejected from the discharge hole, and the constantly cooled electrolytic solution is supplied to the surface to be processed, and the object to be processed is efficiently cooled. It is thought to be for this purpose.

本実施例では吐出孔を円形としたが、溝の延びる方向に広がったスリット状の吐出孔とする等の変更も当然に可能である。また、ピストンWのピストンリング溝W1に加えてピストンリング溝W2にも酸化被膜を形成するようにしてもよい。   In the present embodiment, the discharge hole is circular, but it is of course possible to change it to a slit-like discharge hole that spreads in the direction in which the groove extends. In addition to the piston ring groove W1 of the piston W, an oxide film may be formed on the piston ring groove W2.

本発明の陽極酸化処理装置の機能説明図である。It is function explanatory drawing of the anodizing apparatus of this invention. 電極部縦断面図である。It is an electrode part longitudinal cross-sectional view. 電極部平面図である。It is an electrode part top view. 基板縦断面図である。It is a board | substrate longitudinal cross-sectional view. 基板平面図である。It is a board | substrate top view. 中板縦断面図である。It is a middle board longitudinal cross-sectional view. 中板平面図である。It is a middle board top view. 電極本体縦断面図である。It is an electrode main body longitudinal cross-sectional view. 電極本体平面図である。It is an electrode main body top view.

符号の説明Explanation of symbols

1:保持手段 11:減速モーター 12:保持軸
W:被処理物(ピストン) W1:第一溝部 W2:第二溝部
W3:第三溝部 W5:マスキング 2:電極部 21:基板
22:中板 23:電極本体 233:通孔 234:吐出孔
3.電解槽 4:供給手段 41:冷却槽 412:冷却手段
413:温度制御手段 43:ポンプ 44:流量制御手段 45.パイプ
1: Holding means 11: Deceleration motor 12: Holding shaft W: Object to be processed (piston) W1: First groove W2: Second groove W3: Third groove W5: Masking 2: Electrode 21: Substrate 22: Middle plate 23 : Electrode body 233: Through hole 234: Discharge hole 3. Electrolysis tank 4: Supply means 41: Cooling tank 412: Cooling means 413: Temperature control means 43: Pump 44: Flow rate control means 45. pipe

Claims (6)

側周面の被処理面にリング状の凹部を持つ筒状の被処理物に電流を通電する第1電極部と、
該第1電極部との間に電圧が印加される電極本体を有する第2電極部と、
前記第2電極部を通して電解液を供給する電解液供給手段と、
前記第1電極部と前記第2電極部との間前記電圧を印加する通電手段と、
を備える陽極酸化処理装置において、
前記電極本体は、前記被処理面を囲むように対向する内周面、及び該内周面を周壁とし上面が開口した液槽を有し、
該内周面には、前記凹部に対向し該凹部に向かって電解液を噴射する複数の吐出孔を有することを特徴とする陽極酸化処理装置。
A first electrode portion for supplying current to a cylindrical workpiece having a ring-shaped concave portion on a processing surface of a side peripheral surface;
A second electrode part having an electrode body to which a voltage is applied between the first electrode part ;
An electrolytic solution supply means that teapot subjected electrolyte through the second electrode portions,
Energizing means for applying said voltage between said first electrode portion and the second electrode portions,
In an anodizing apparatus comprising:
The electrode body has an inner peripheral surface facing so as to surround the surface to be processed, and a liquid tank whose upper surface is open with the inner peripheral surface as a peripheral wall,
An anodizing apparatus characterized in that the inner peripheral surface has a plurality of discharge holes that are opposed to the recess and inject an electrolyte toward the recess .
前記第1電極部には、前記被処理物を前記被処理物の軸を中心として回転させる回転手段が設けられている、ことを特徴とする請求項に記載の陽極酸化処理装置。 Wherein the first electrode portion, anodization apparatus according the rotating means for rotating the object to be treated about the axis of the object to be processed is provided, in claim 1 you characterized. 前記第2電極部は、前記液槽の下方に電解液が供給されるチャンバーを有し、前記第2電極部に供給される電解液は、前記チャンバー、及び前記電極本体に設けられた電解液通路を介して、前記吐出孔から噴射される、ことを特徴とする請求項1又は2に記載の陽極酸化処理装置。 The second electrode part has a chamber in which an electrolytic solution is supplied below the liquid tank, and the electrolytic solution supplied to the second electrode part is an electrolytic solution provided in the chamber and the electrode body. The anodizing apparatus according to claim 1, wherein the anodizing apparatus is ejected from the discharge hole through a passage. 請求項1〜3の何れか1項に記載の陽極酸化処理装置において、  In the anodizing apparatus according to any one of claims 1 to 3,
前記液槽の上方からオーバーフローした電解液を回収する電解槽と、  An electrolytic cell for collecting the electrolytic solution overflowed from above the liquid cell;
該電解槽から供給された電解液を冷却する冷却槽とを備え、  A cooling tank for cooling the electrolytic solution supplied from the electrolytic tank,
前記電解液供給手段は、前記冷却槽で冷却された電解液を前記第2電極部へ供給する、  The electrolytic solution supply means supplies the electrolytic solution cooled in the cooling tank to the second electrode unit.
ことを特徴とする陽極酸化処理装置。An anodizing apparatus characterized by that.
前記電解液供給手段は、電解液を貯留する貯留槽と、該貯留槽と前記電解液通路とを接続する流入路と、該流入路に配置され前記貯留槽から前記電解液通路に電解液を送出するポンプと、を有する請求項1〜4のいずれか1項に記載の陽極酸化処理装置。 The electrolyte supply means includes a storage tank that stores the electrolyte, an inflow path that connects the storage tank and the electrolyte passage, and an electrolyte that is disposed in the inflow path from the storage tank to the electrolyte path. The anodizing apparatus according to any one of claims 1 to 4 , further comprising: a pump for delivery. 前記貯留槽は、前記被処理物に噴射された後の電解液を受ける開口部を持つ請求項に記載の陽極酸化処理装置。 The anodizing apparatus according to claim 5 , wherein the storage tank has an opening for receiving the electrolytic solution after being sprayed on the object to be processed.
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JP2004043873A (en) * 2002-07-10 2004-02-12 Aisin Keikinzoku Co Ltd Method for surface treatment of aluminum alloy
JP2004059936A (en) * 2002-07-24 2004-02-26 Aisin Keikinzoku Co Ltd Surface treatment apparatus for aluminum alloy

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