JP5803573B2 - Anodizing equipment - Google Patents

Anodizing equipment Download PDF

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JP5803573B2
JP5803573B2 JP2011236722A JP2011236722A JP5803573B2 JP 5803573 B2 JP5803573 B2 JP 5803573B2 JP 2011236722 A JP2011236722 A JP 2011236722A JP 2011236722 A JP2011236722 A JP 2011236722A JP 5803573 B2 JP5803573 B2 JP 5803573B2
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electrolyte
guide plate
electrolytic solution
electrode
anodizing
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JP2013095925A (en
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修 小日向
修 小日向
久隆 高木
久隆 高木
和仁 西垣
和仁 西垣
徹太郎 中川
徹太郎 中川
誠喜 加藤
誠喜 加藤
岳世 和田
岳世 和田
正夫 筒井
正夫 筒井
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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、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.

一般的に陽極酸化処理は、通電を確保するため酸化処理電解液(以下電解液と呼ぶ)の液面下で行う。被処理物表面の一部に陽極酸化処理を行う場合は、陽極酸化処理を行わない非処理部に電解液が接触しないようにする必要がある。例えば、アルミニウム基金属製被処理物表面の一部に陽極酸化処理を施す場合には、被処理物表面に弾性体のマスキング材料を取り付けて電解液と接触しないようにカバーする方法が知られている(例えば、特許文献1参照。)。   In general, the anodizing treatment is performed below the surface of an oxidizing electrolytic solution (hereinafter referred to as an electrolytic solution) in order to ensure energization. When anodizing is performed on a part of the surface of the object to be processed, it is necessary to prevent the electrolytic solution from coming into contact with the non-treated portion where the anodizing is not performed. For example, when anodizing is performed on a part of the surface of an aluminum-based metal workpiece, a method is known in which an elastic masking material is attached to the surface of the workpiece to cover it so that it does not come into contact with the electrolyte. (For example, refer to Patent Document 1).

また、マスキングを行わずに被処理物表面の一部に陽極酸化処理を施す方法として、例えば陽極酸化処理部と非処理部との境界を電解液の液面で分離して確保する方法が知られている(例えば、特許文献2参照。)。   In addition, as a method for anodizing a part of the surface of an object to be processed without masking, for example, a method is known in which the boundary between the anodized portion and the non-treated portion is separated and secured at the electrolyte surface. (For example, see Patent Document 2).

特開2006−336050号公報JP 2006-336050 A 特開平11−12781号公報JP-A-11-12781

しかしながら特許文献1のマスキング方法では、マスキング材料が必要となる一方、被処理物の表面にマスキング材料を取り付けたり、外したりするための工程、作業、時間が必要となる。このため、陽極酸化処理の生産性が悪くなり、コスト高になる問題がある。   However, while the masking method of Patent Document 1 requires a masking material, it requires a process, work, and time for attaching or removing the masking material on the surface of the workpiece. For this reason, there is a problem that the productivity of the anodizing treatment is deteriorated and the cost is increased.

また、特許文献2の液面で境界を確保する方法は、電解液を攪拌したり、補充したりする際に発生する液面の変動によって陽極酸化処理部と非処理部との境界が不安定になり、確実な境界が確保できない問題がある。   Further, in the method of securing the boundary at the liquid level in Patent Document 2, the boundary between the anodized portion and the non-treated portion is unstable due to the fluctuation of the liquid level that occurs when the electrolyte is stirred or replenished. Therefore, there is a problem that a certain boundary cannot be secured.

本発明は上記問題点に鑑みて成されたものであり、マスキング材料を使用せずに被処理物の目的とする表面部分に陽極酸化処理を施すことができる陽極酸化処理装置を提供することを目的とする。   The present invention has been made in view of the above problems, and provides an anodizing apparatus capable of anodizing a target surface portion of an object to be processed without using a masking material. Objective.

本発明の第1の課題解決手段は、周面にリング状の溝部を有する金属製の被処理物に接触し電流を通電する第1電極部と、前記被処理物と対向する電解液吐出孔と、前記吐出孔から吐出し前記被処理物の表面と接触した状態にある電解液を貯留する貯留部と、前記電解液吐出孔に電解液を供給する電解液通路と、を有する第2電極部と、前記貯留部から過剰となった電解液を排出する電解液排出手段と、前記電解液通路へ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電極部とに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、前記電解液排出手段は、電解液を取り入れる取入口と、電解液を流す流路と、を有し、前記流路は、前記電解液排出手段の回転中心から放射状に誘導板を備えており、前記誘導板は、前記被処理物と一体に回転することを特徴とする構成である。 The first problem-solving means of the present invention includes a first electrode portion that contacts a metal workpiece having a ring-shaped groove on its peripheral surface and energizes current, and an electrolyte discharge hole that faces the workpiece. A second electrode having a storage portion for storing the electrolyte solution discharged from the discharge hole and in contact with the surface of the object to be processed; and an electrolyte passage for supplying the electrolyte solution to the electrolyte solution discharge hole An electrolyte solution discharging means for discharging an excess electrolyte solution from the storage portion, an electrolyte supply means for supplying an electrolyte solution to the electrolyte passage, the first electrode portion, and the second electrode portion In the anodizing apparatus comprising: an energization means for applying a voltage to the electrolyte solution, the electrolyte discharge means includes an intake port for taking in the electrolyte solution, and a flow channel for flowing the electrolyte solution, A guide plate is provided radially from the rotation center of the electrolyte discharging means, and the guide plate A construction which is characterized in that rotate integrally with the object to be processed.

本発明の第2の課題解決手段は、前記電解液排出手段は、前記誘導板と、前記誘導板の上部に設けられるリング状の上部案内部と、前記誘導板の下部に設けられるリング状の下部案内部と、からなる、構成である。 According to a second problem-solving means of the present invention, the electrolyte discharge means includes the guide plate, a ring-shaped upper guide portion provided on the upper portion of the guide plate, and a ring-shape provided on the lower portion of the guide plate. And a lower guide part .

本発明の陽極酸化装置では、陽極酸化処理のために被処理物を第1電極部と接触させ、被処理物と対向している第2電極部の電解液吐出孔から電解液供給手段で電解液を吐出させ、被処理物の表面と電解液を接触した状態で通電手段により第1電極部と第2電極部との間に電圧を印加すると、第1電極部と接触した被処理物と第2電極部の間に電解液を介して電流が流れ、被処理物の表面は電解液に接触した部分に陽極酸化処理を施すことができる。また、吐出孔から吐出した電解液は被処理物と接触した状態で貯留部に貯まり、この際に電解液排出手段により貯留部から過剰となった電解液が排出され、所定の高さ以上は被処理物の表面と電解液が接触せず陽極酸化処理が施されない。以上のことから、本発明の陽極酸化装置ではマスキング材料を使用せずに被処理物の表面の目的とした部分に陽極酸化処理を施すことができる。   In the anodizing apparatus of the present invention, the object to be treated is brought into contact with the first electrode part for anodizing treatment, and electrolysis is performed by the electrolyte solution supply means from the electrolyte discharge hole of the second electrode part facing the object to be treated. When a voltage is applied between the first electrode part and the second electrode part by the energizing means in a state where the liquid is discharged and the surface of the object to be processed is in contact with the electrolytic solution, the object to be processed in contact with the first electrode part An electric current flows between the second electrode portions via the electrolytic solution, and the surface of the object to be processed can be subjected to an anodizing treatment at a portion in contact with the electrolytic solution. In addition, the electrolyte discharged from the discharge hole is stored in the storage part in contact with the object to be processed, and at this time, excess electrolyte is discharged from the storage part by the electrolyte discharge means, The surface of the object to be processed and the electrolytic solution do not come into contact with each other and the anodizing treatment is not performed. From the above, in the anodizing apparatus of the present invention, an anodizing treatment can be performed on a target portion of the surface of the object to be processed without using a masking material.

また、貯留部に貯留した電解液が過剰となると、過剰となった電解液は取入口から取り入れられ、取り入れられた電解液は流路を流れて移動することができるので、過剰となった電解液を次々と排出することができる。   Also, if the electrolyte stored in the reservoir becomes excessive, the excess electrolyte can be taken in from the intake, and the introduced electrolyte can move through the flow path, so the excess electrolyte The liquid can be discharged one after another.

また、電解液排出手段を回転させると、前記電解液排出手段が備える放射状の板が取り入れた電解液を回転方向に押し出し、押し出された電解液には遠心力が働くので放射状の誘導板に沿って回転中心から外へ流れて移動し、さらに電解液を排出することができる。   Further, when the electrolyte discharging means is rotated, the electrolyte taken in by the radial plate provided in the electrolyte discharging means is pushed out in the rotation direction, and centrifugal force acts on the extruded electrolyte so that it follows the radial induction plate. As a result, the electrolyte flows out of the center of rotation and moves, and the electrolyte can be discharged.

また、被処理物の表面と電解液の接触状態が違っていても被処理物を回転させることにより被処理物の表面と電解液の接触状態を一定にすることで、被処理物の表面に一定の陽極酸化処理を施すことができる。   Moreover, even if the contact state between the surface of the object to be processed and the electrolytic solution is different, the contact state between the surface of the object to be processed and the electrolytic solution is made constant by rotating the object to be processed, so that the surface of the object to be processed A certain anodizing treatment can be performed.

本発明の実施形態に係る陽極酸化処理装置の説明図である。It is explanatory drawing of the anodizing apparatus which concerns on embodiment of this invention. 本発明の実施形態に係る電極部の部分拡大図である。It is the elements on larger scale of the electrode part which concerns on embodiment of this invention. 本発明の実施形態に係る電極部の平面図である。It is a top view of the electrode part which concerns on embodiment of this invention. 本発明の実施形態に係る基盤の部分拡大図である。It is the elements on larger scale of the base | substrate which concerns on embodiment of this invention. 本発明の実施形態に係る基盤の平面図である。It is a top view of the base concerning an embodiment of the present invention. 本発明の実施形態に係る中板の部分拡大図である。It is the elements on larger scale of the middle board concerning the embodiment of the present invention. 本発明の実施形態に係る中板の平面図である。It is a top view of the middle board concerning the embodiment of the present invention. 本発明の実施形態に係る電極本体の部分拡大図である。It is the elements on larger scale of the electrode main body which concerns on embodiment of this invention. 本発明の実施形態に係る電極本体の平面図である。It is a top view of the electrode main body concerning the embodiment of the present invention. 本発明の実施形態に係る羽根車部の部分拡大図である。It is the elements on larger scale of the impeller part which concerns on embodiment of this invention. 本発明の実施形態に係る羽根車部の平面図である。It is a top view of the impeller part concerning the embodiment of the present invention.

以下に本発明の実施形態を図面に基づいて詳細に説明する。   Embodiments of the present invention will be described below in detail with reference to the drawings.

図1は、本発明の実施形態に係る陽極酸化処理装置1の説明図である。本実施形態の陽極酸化処理装置1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を含む側周面Wfを主として陽極酸化処理するものである。前記陽極酸化処理装置1は、保持手段2(第1電極部)と、電極部3(第2電極部)と、羽根車部4(電解液排出手段)と、電解液供給手段5と、通電手段6と、電解槽7と、貯留部8と、を有する。   FIG. 1 is an explanatory diagram of an anodizing apparatus 1 according to an embodiment of the present invention. The anodizing apparatus 1 according to the present embodiment is for anodizing a piston ring groove W1 of a piston W made of an aluminum alloy. More precisely, of the three piston ring grooves W1, W2 and W3 formed from the top portion on the outer peripheral surface of the top portion of the piston W to the skirt portion, the side peripheral surface Wf including the piston ring groove W1 on the top portion side is mainly used. Anodizing treatment is performed. The anodizing apparatus 1 includes a holding means 2 (first electrode part), an electrode part 3 (second electrode part), an impeller part 4 (electrolyte discharging means), an electrolyte supply means 5, Means 6, electrolytic cell 7, and reservoir 8 are included.

保持手段2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21と、この減速モータ21の出力軸に固定された保持軸22と、保持軸22の下端に設けられたピストンWの内周面に着脱自在に係止する係止爪(図示せず)と、からなる。保持軸22の軸方向中程には羽根車部4を着脱自在に固定することができる円筒状の支持具23が取り付けてあり、この支持具23は保持軸22の上下方向に自由に位置を変えることができる。前記係止爪は、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22とピストンW及び羽根車部4は同軸となる。   The holding means 2 includes a reduction motor 21 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 22 fixed to an output shaft of the reduction motor 21. And a locking claw (not shown) that is detachably locked to the inner peripheral surface of the piston W provided at the lower end of the holding shaft 22. In the middle of the holding shaft 22 in the axial direction, a cylindrical support tool 23 that can removably fix the impeller portion 4 is attached. The support tool 23 is freely positioned in the vertical direction of the holding shaft 22. Can be changed. 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 22, the piston W, and the impeller portion 4 are coaxial.

また、保持軸22の支持具23より上方に、通電手段6を構成する集電リング61が固定され、この集電リング61と前記係止爪とは電気的に通電し、かつ前記係止爪を介してピストンWに通電している。集電リング61と、保持軸22と、ピストンWとにより陽極が構成される。   A current collecting ring 61 constituting the energizing means 6 is fixed above the support 23 of the holding shaft 22, and the current collecting ring 61 and the locking claw are electrically energized, and the locking claw The piston W is energized via The current collecting ring 61, the holding shaft 22, and the piston W constitute an anode.

電解液供給手段5は、電解槽7から回収された電解液を所定の温度に冷却するための冷却槽51と、電解液を送り出す駆動手段であるポンプ52と、電解液の流量を制御する流量計53と、ポンプ52から圧送される電解液を通すパイプ54から構成される。さらに冷却槽51には、電解液を貯留するサブタンク511と、回収された電解液を冷却する冷凍機512及び熱交換器513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514が設けられている。なお、パイプ54は、本発明の流入路を構成するものである。   The electrolytic solution supply means 5 includes a cooling tank 51 for cooling the electrolytic solution recovered from the electrolytic tank 7 to a predetermined temperature, a pump 52 that is a driving means for sending the electrolytic solution, and a flow rate for controlling the flow rate of the electrolytic solution. It is composed of a total 53 and a pipe 54 through which the electrolytic solution pumped from the pump 52 is passed. Further, the cooling tank 51 includes a sub tank 511 for storing the electrolytic solution, a refrigerator 512 and a heat exchanger 513 for cooling the recovered electrolytic solution, and a temperature sensor 514 that constitutes a control means for controlling the temperature of the electrolytic solution. Is provided. The pipe 54 constitutes the inflow path of the present invention.

電解槽7は、上端開口する容器状のものであり、電解槽7の底に受け溜まった電解液を電解液供給手段5に回収させる回収口71が設けられている。さらに、電解槽7の上端開口部は、電解液の飛散を防止するための円環状の鍔72が設けられている。   The electrolytic cell 7 is a container having an opening at the upper end, and is provided with a recovery port 71 for allowing the electrolytic solution supply means 5 to collect the electrolytic solution collected at the bottom of the electrolytic cell 7. Furthermore, the upper end opening of the electrolytic cell 7 is provided with an annular collar 72 for preventing the electrolyte from scattering.

図2は、本発明の実施形態に係る電極部3の部分拡大図であって、図3は、本発明の実施形態に係る電極部3の平面図である。電極部3は、電極部3の土台となる方形状の基板31と、基板31の上方に設けられる円盤状の中板32と、中板32の上方に設けられるリング状の電極本体33と、電極本体33に接した状態で中板32に組み込まれ右方向に延出し通電手段6と接続される導体34と、から構成され、陽極酸化処理装置1の陰極を構成するものである。また、中板32と電極本体33と導体34は、内側部分に電解液を貯留する貯留部8を形成する。   FIG. 2 is a partially enlarged view of the electrode unit 3 according to the embodiment of the present invention, and FIG. 3 is a plan view of the electrode unit 3 according to the embodiment of the present invention. The electrode unit 3 includes a rectangular substrate 31 serving as a base of the electrode unit 3, a disk-shaped intermediate plate 32 provided above the substrate 31, a ring-shaped electrode main body 33 provided above the intermediate plate 32, The conductor 34 is incorporated in the middle plate 32 in contact with the electrode body 33 and extends rightward and connected to the energizing means 6, and constitutes the cathode of the anodizing apparatus 1. Further, the intermediate plate 32, the electrode main body 33, and the conductor 34 form a storage portion 8 that stores the electrolytic solution in the inner portion.

図4は、本発明の実施形態に係る基盤31の部分拡大図であって、図5は、本発明の実施形態に係る基盤31の平面図であるある。基板31は、4隅を丸く形成された方形の板状で、その上面に浅い円形の第1円形凹部311と、その第1円形凹部311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312と、を備える。   FIG. 4 is a partially enlarged view of the base 31 according to the embodiment of the present invention, and FIG. 5 is a plan view of the base 31 according to the embodiment of the present invention. The substrate 31 has a rectangular plate shape with rounded four corners. A shallow circular first circular recess 311 is formed on the upper surface of the substrate 31, and one end is opened at the center of the first circular recess 311 and the other end is opened on a side surface. A tunnel-shaped passage 312.

図6は、本発明の実施形態に係る中板32の部分拡大図であって、図7は、本発明の実施形態に係る中板32の平面図である。中板32は、円盤状でその下面側には中央部に浅い円形の第2円形凹部321を形成する突条322と、上面側の中央部に浅い円形の第1円形溝323と、これと同軸の浅い円形の第2円形溝324を形成する段付突条325を備える。さらに下面側の第2円形凹部321と上面側の第2円形溝324とに両端が開口する通孔326が形成されている。通孔326は、等間隔のリング状に8個設けられている。さらに中板32には、その外周面から第1円形溝323に表出する導体34が組み込まれている。   FIG. 6 is a partially enlarged view of the intermediate plate 32 according to the embodiment of the present invention, and FIG. 7 is a plan view of the intermediate plate 32 according to the embodiment of the present invention. The intermediate plate 32 has a disc shape and has a protrusion 322 that forms a shallow circular second circular recess 321 at the center on the lower surface side, a shallow circular first circular groove 323 at the center on the upper surface side, and A stepped ridge 325 that forms a second coaxially shallow circular groove 324 is provided. Furthermore, through holes 326 having both ends opened are formed in the second circular recess 321 on the lower surface side and the second circular groove 324 on the upper surface side. Eight through holes 326 are provided in a ring shape at equal intervals. Further, a conductor 34 that is exposed to the first circular groove 323 from the outer peripheral surface thereof is incorporated in the intermediate plate 32.

図8は、本発明の実施形態に係る電極本体33の部分拡大図であって、図9は、本発明の実施形態に係る電極本体33の平面図である。電極本体33は、外周部が2段となる段付き円筒状であり、リング状の下面331に開口する8個の流入孔333と流入孔333に連通し電極本体33の内周面332に開口する8個の吐出孔334を持つ。流入孔333は中板32に設けられた8個の通孔326と対応する位置にあり、中板32の通孔326と電極本体33の流入孔333及び吐出孔334とは連通するようになり電解液通路となる。流入孔333の内周面332側の開口は電解液の吐出孔334となり、いずれも電極本体33の軸心に向かってオフセットして開口している。このため電解液は、水平方向に軸心に向かってオフセットして吐出する。また、電極本体33の内周面332と中板32の上面側の第1円形溝323は貯留部8を構成するものであり、吐出孔334から吐出した電解液はこの貯留部8に溜めることができる。電極本体33は、中板32と嵌合する際、中板に組み込まれた導体24を介して通電する。   FIG. 8 is a partially enlarged view of the electrode main body 33 according to the embodiment of the present invention, and FIG. 9 is a plan view of the electrode main body 33 according to the embodiment of the present invention. The electrode body 33 has a stepped cylindrical shape with two outer peripheral portions, and communicates with the eight inflow holes 333 that open on the ring-shaped lower surface 331 and the inflow holes 333 and opens on the inner peripheral surface 332 of the electrode body 33. Eight discharge holes 334 are provided. The inflow holes 333 are located at positions corresponding to the eight through holes 326 provided in the intermediate plate 32, and the through holes 326 of the intermediate plate 32 communicate with the inflow holes 333 and the discharge holes 334 of the electrode body 33. It becomes an electrolyte passage. The opening on the inner peripheral surface 332 side of the inflow hole 333 serves as an electrolyte discharge hole 334, and all of the openings are offset toward the axis of the electrode body 33. For this reason, the electrolytic solution is discharged while being offset toward the axial center in the horizontal direction. Further, the inner circumferential surface 332 of the electrode body 33 and the first circular groove 323 on the upper surface side of the intermediate plate 32 constitute the storage portion 8, and the electrolyte discharged from the discharge holes 334 is stored in the storage portion 8. Can do. The electrode main body 33 is energized through the conductor 24 incorporated in the intermediate plate when fitted to the intermediate plate 32.

図10は、本発明の実施形態に係る羽根車部4の部分拡大図であって、図11は、本発明の実施形態に係る羽根車部4の平面図である。羽根車部4は、羽根板41と、羽根板41の上部に設けられるリング状の上部案内板42と、羽根板42の下部に設けられるリング状の下部案内板43と、からなる。上部案内板42と下部案内板43は、中心軸を同じにして下部案内板43は電極本体33の上面と平行に、上部案内板42は下部案内板43との距離が内径部から外径部に向かって広くなるように設けられている。また、下部案内板43の内径を上部案内板42の内径より大きくして環状開口部44が設けられており、この環状開口部44から電解液が取り入れられる。羽根板41は、上部案内板42と下部案内板43の間に前記中心軸から放射状に等間隔に配置されて上部案内板42と下部案内板43を接合している。また、羽根板41と上部案内板42と下部案内板43とから電解液を流す流路45が構成されている。羽根車部4は、上部案内板42の上面に結合し保持手段2に固定される円筒状の支持具23を介して、保持軸22に固定され、一体に回転する。   FIG. 10 is a partially enlarged view of the impeller unit 4 according to the embodiment of the present invention, and FIG. 11 is a plan view of the impeller unit 4 according to the embodiment of the present invention. The impeller unit 4 includes a blade plate 41, a ring-shaped upper guide plate 42 provided on the upper portion of the blade plate 41, and a ring-shaped lower guide plate 43 provided on the lower portion of the blade plate 42. The upper guide plate 42 and the lower guide plate 43 have the same central axis, the lower guide plate 43 is parallel to the upper surface of the electrode body 33, and the upper guide plate 42 is spaced from the lower guide plate 43 at a distance from the inner diameter portion to the outer diameter portion. It is provided so as to become wider toward. An annular opening 44 is provided by making the inner diameter of the lower guide plate 43 larger than the inner diameter of the upper guide plate 42, and an electrolytic solution is taken from the annular opening 44. The vane plate 41 is disposed between the upper guide plate 42 and the lower guide plate 43 at equal intervals radially from the central axis, and joins the upper guide plate 42 and the lower guide plate 43. Further, a flow path 45 through which the electrolyte solution flows is constituted by the blade plate 41, the upper guide plate 42 and the lower guide plate 43. The impeller unit 4 is fixed to the holding shaft 22 via a cylindrical support 23 that is coupled to the upper surface of the upper guide plate 42 and fixed to the holding means 2, and rotates integrally.

また、本実施形態では、電解液が吐出孔334からピストンリング溝W1を含む側周面Wfの表面に吐出される際、電極本体33の内周面332と被処理面を構成するピストンリング溝W1との距離は陽極酸化処理の効果に影響する。すなわちピストンリング溝W1を含む側周面Wfが、陰極となる電極本体33の内周面332に近すぎるとショートする恐れが生じる。逆にピストンリング溝W1を含む側周面Wfと電極本体33の内周面332間の距離が離れすぎると電解液が有効にピストンリング溝W1を含む側周面Wf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リング溝W1を含む側周面Wfから電極本体33の吐出孔334間の距離が2.0〜15.0mmであることが好ましい。   Further, in the present embodiment, when the electrolyte is discharged from the discharge hole 334 to the surface of the side peripheral surface Wf including the piston ring groove W1, the piston ring groove constituting the inner peripheral surface 332 of the electrode body 33 and the surface to be processed. The distance from W1 affects the effect of the anodizing treatment. That is, if the side peripheral surface Wf including the piston ring groove W1 is too close to the inner peripheral surface 332 of the electrode main body 33 serving as the cathode, there is a risk of short circuit. Conversely, if the distance between the side peripheral surface Wf including the piston ring groove W1 and the inner peripheral surface 332 of the electrode body 33 is too large, the electrolyte does not reach the side peripheral surface Wf including the piston ring groove W1 effectively, and anodization is performed. Processing is insufficient. Therefore, it is preferable that the distance between the discharge hole 334 of the electrode body 33 from the side peripheral surface Wf including the piston ring groove W1 connected to the anode is 2.0 to 15.0 mm.

ピストンWの回転は、アルマイト皮膜を均一に形成する作用を持つが、必要以上に回転を上げると電解液が飛散防止用の円環状の鍔72を超えて飛散するため、回転数を10〜800rpmに設定することが好ましい。   The rotation of the piston W has the effect of uniformly forming the alumite film. However, if the rotation is increased more than necessary, the electrolyte will be scattered beyond the annular collar 72 for preventing scattering. It is preferable to set to.

電解液として硫酸濃度が150g/ルットル〜600g/リットルである硫酸水溶液を利用し、電解液の流量は1リットル/分〜6リットル/分で、さらに、電流密度は1A/dm2〜100A/dm2で、電圧は15V〜90Vである。   A sulfuric acid aqueous solution having a sulfuric acid concentration of 150 g / l to 600 g / l is used as the electrolytic solution, the flow rate of the electrolytic solution is 1 liter / minute to 6 liter / minute, and the current density is 1 A / dm2 to 100 A / dm2. The voltage is 15V to 90V.

保持手段2の材質は、通電性を必要とするため、通電性のよい金属材料が好ましい。   Since the material of the holding means 2 requires electrical conductivity, a metal material with good electrical conductivity is preferable.

電解槽7の材質は、電解液に接触するため耐酸性が必要とされ、塩化ビニル製またはSUS316製が好ましい。   The material of the electrolytic cell 7 is required to be acid resistant because it contacts the electrolytic solution, and is preferably made of vinyl chloride or SUS316.

基板31の材質は、電解液と接触するため耐腐食性のある材料が好ましく、更に言えば電解液は強酸を用いる場合が多いため耐酸性のある、例えばSUS316製が使用できる。   The material of the substrate 31 is preferably a corrosion-resistant material because it comes into contact with the electrolytic solution. Furthermore, since the electrolytic solution often uses a strong acid, an acid-resistant material such as SUS316 can be used.

中板32の材質は、電気を漏電させないための絶縁性と電解液に接触するための耐酸性が必要とされ耐腐食性のある高分子材料が好ましく、例えば塩化ビニル製が使用できる。   The material of the intermediate plate 32 is preferably a high-corrosion-resistant polymer material that requires insulation for preventing leakage of electricity and acid resistance for contact with the electrolytic solution. For example, vinyl chloride can be used.

電極本体33と導体34の材質は、電気を通すための通電性と電解液に接触するための耐酸性が必要とされ、例えばSUS316製が使用できる。   The material of the electrode body 33 and the conductor 34 is required to have electrical conductivity for conducting electricity and acid resistance for contacting the electrolytic solution. For example, SUS316 can be used.

羽根車部4の材質は陽極酸化機能を阻害しないよう保持手段2や電極部3と絶縁されていることが好ましく、さらに、電解液に接触し電解液の流動による力に耐え得る必要から、耐酸性のある高強度の高分子材料が好ましく、例えばガラス繊維入りの四フッ化エチレン樹脂製が使用できる。   The material of the impeller part 4 is preferably insulated from the holding means 2 and the electrode part 3 so as not to impede the anodizing function. Further, since the impeller part 4 needs to be able to withstand the force caused by the flow of the electrolytic solution by contacting the electrolytic solution, A high-strength high-molecular material is preferable. For example, a glass fiber-containing tetrafluoroethylene resin can be used.

本発明の実施形態の動作について説明する。電解液供給手段5に組み込まれている冷却槽51で冷却された電解液は、流量計53により流量が制御され、ポンプ52により電極部3に送られる。電解液は、電極部3にある基板31のトンネル状の通路312から、基板31の上面側の第1円形凹部311と中板32の下部の第2円形凹部321間からなる空間を通り、中板32の通孔326と電極本体33の通孔333を通過し、吐出孔334からピストンリング溝W1を含む側周面Wfに吐出される。さらに、電解液は、吐出孔334から吐出され、陽極酸化処理が行われた後、電極本体33の内周面332と、中板32の第1円形溝323と、から構成される貯留部8に溜まり満たしていく。貯留部8から過剰となった電解液は、回転する羽根車部4の環状開口部44から羽根車部4内に入り上部案内板42と下部案内板43と羽根板41とから構成される流路45を通って羽根車部4の外径部から流出し、電解槽7の底の回収穴71を通じて、電解液供給手段5の冷却槽51に回収される。そして、回収された電解液は、電解液供給手段5が保有する熱交換器513により冷却され、再び電極部3に送られる。   The operation of the embodiment of the present invention will be described. The flow rate of the electrolytic solution cooled in the cooling tank 51 incorporated in the electrolytic solution supply means 5 is controlled by the flow meter 53 and sent to the electrode unit 3 by the pump 52. The electrolyte passes through a space between the first circular recess 311 on the upper surface side of the substrate 31 and the second circular recess 321 on the lower side of the intermediate plate 32 from the tunnel-shaped passage 312 of the substrate 31 in the electrode unit 3. It passes through the through hole 326 of the plate 32 and the through hole 333 of the electrode body 33 and is discharged from the discharge hole 334 to the side peripheral surface Wf including the piston ring groove W1. Further, after the electrolytic solution is discharged from the discharge hole 334 and subjected to anodizing treatment, the reservoir 8 constituted by the inner peripheral surface 332 of the electrode body 33 and the first circular groove 323 of the intermediate plate 32. It accumulates and fills up. Excess electrolyte from the storage unit 8 enters the impeller unit 4 through the annular opening 44 of the rotating impeller unit 4 and is composed of the upper guide plate 42, the lower guide plate 43, and the vane plate 41. It flows out from the outer diameter part of the impeller part 4 through the path 45 and is collected in the cooling tank 51 of the electrolytic solution supply means 5 through the recovery hole 71 at the bottom of the electrolytic tank 7. The recovered electrolytic solution is cooled by the heat exchanger 513 held by the electrolytic solution supply means 5 and sent to the electrode unit 3 again.

羽根車部4は、保持軸22に結合されて保持軸22と一体に回転している。羽根車部4を回転させると、貯留部8から過剰となった電解液は、環状開口部44に取り入れられ、羽根車部4の外径部に押し流されて移動する。この移動により環状開口部44から新たな電解液が吸い込まれ、移動した電解液は電解槽7に放出される。このように羽根車部4を回転させると電解液を吸い込んで放出するポンプの役目をするので所定の高さ以上にある電解液を排出して一定の液面Hを確保している。   The impeller unit 4 is coupled to the holding shaft 22 and rotates integrally with the holding shaft 22. When the impeller part 4 is rotated, the excess electrolyte from the storage part 8 is taken into the annular opening 44 and is moved by being swept away by the outer diameter part of the impeller part 4. By this movement, a new electrolytic solution is sucked from the annular opening 44 and the moved electrolytic solution is discharged to the electrolytic cell 7. When the impeller portion 4 is rotated in this manner, it functions as a pump that sucks and discharges the electrolyte solution, so that the electrolyte solution at a predetermined height or higher is discharged to ensure a constant liquid level H.

本発明の実施形態の効果について説明する。   The effect of the embodiment of the present invention will be described.

本発明の陽極酸化装置1では、陽極酸化処理のためにピストンWを保持手段2と接触させ、ピストンリング溝W1を含む側周面Wfと対向している電極部3の吐出孔334から電解液供給手段5で電解液を吐出させ、ピストンリング溝W1を含む側周面Wfの表面と電解液を接触した状態で通電手段6により保持手段2と電極部3との間に電圧を印加すると、保持手段2と接触したピストンリング溝W1を含む側周面Wfと電極部3の間に電解液を介して電流が流れ、ピストンリング溝W1を含む側周面Wfの表面の電解液に接触した部分に陽極酸化処理を施すことができる。また、吐出孔334から吐出した電解液は、ピストンリング溝W1を含む側周面Wfと接触した状態で貯留部8に貯まり、この際に羽根車部4により貯留部8から過剰となった電解液が排出され、所定の高さの液面H以上は、ピストンリング溝W1を含む側周面Wfの表面と電解液が接触せず陽極酸化処理が施されない。以上のことから、本発明の陽極酸化装置1ではマスキング材料を使用せずにピストンリング溝W1を含む側周面Wfの表面の目的とした部分に陽極酸化処理を施すことができる。   In the anodizing device 1 of the present invention, the electrolyte W is supplied from the discharge hole 334 of the electrode portion 3 that is in contact with the holding means 2 and is opposed to the side peripheral surface Wf including the piston ring groove W1 for anodizing treatment. When the electrolytic solution is discharged by the supply means 5 and a voltage is applied between the holding means 2 and the electrode portion 3 by the energizing means 6 in a state where the electrolytic solution is in contact with the surface of the side peripheral surface Wf including the piston ring groove W1, An electric current flows between the side peripheral surface Wf including the piston ring groove W1 in contact with the holding means 2 and the electrode portion 3 via the electrolytic solution, and contacts the electrolytic solution on the surface of the side peripheral surface Wf including the piston ring groove W1. The part can be anodized. Further, the electrolyte discharged from the discharge hole 334 is stored in the storage portion 8 in a state of being in contact with the side peripheral surface Wf including the piston ring groove W1, and at this time, the electrolysis that has become excessive from the storage portion 8 by the impeller portion 4 The liquid is discharged, and the surface of the side peripheral surface Wf including the piston ring groove W1 is not in contact with the electrolytic solution above the liquid level H having a predetermined height, and the anodizing treatment is not performed. From the above, in the anodizing apparatus 1 of the present invention, an anodizing process can be performed on a target portion of the surface of the side peripheral surface Wf including the piston ring groove W1 without using a masking material.

また、貯留部8に貯留した電解液が過剰となると、過剰となった電解液は、環状開口部44から取り入れられ、取り入れられた電解液は流路45を流れて移動することができるので、過剰となった電解液を次々と排出することができる。   Further, when the electrolyte stored in the storage portion 8 becomes excessive, the excess electrolyte is taken in from the annular opening 44, and the introduced electrolyte can flow through the flow path 45 and move. Excess electrolyte solution can be discharged one after another.

また、羽根車部4を回転させると、羽根車部4が備える放射状の羽根板41が取り入れた電解液を回転方向に押し出し、押し出された電解液には遠心力が働くので放射状の羽根板41に沿って回転中心から外へ流れて移動し、さらに電解液を排出することができる。   Further, when the impeller unit 4 is rotated, the electrolyte solution taken in by the radial blade plate 41 included in the impeller unit 4 is pushed out in the rotation direction, and the centrifugal force acts on the extruded electrolyte solution. , And the electrolyte solution can be discharged.

また、ピストンリング溝W1を含む側周面Wfの表面と電解液の接触状態が違っていてもピストンリング溝W1を含む側周面Wfを回転させることによりピストンリング溝W1を含む側周面Wfの表面と電解液の接触状態を一定にすることでピストンリング溝W1を含む側周面Wfの表面に一定の陽極酸化処理を施すことができる。   Further, even if the contact state between the surface of the side peripheral surface Wf including the piston ring groove W1 and the electrolyte is different, the side peripheral surface Wf including the piston ring groove W1 is rotated by rotating the side peripheral surface Wf including the piston ring groove W1. By making the contact state between the surface and the electrolytic solution constant, the surface of the side peripheral surface Wf including the piston ring groove W1 can be subjected to constant anodic oxidation.

さらに、電解液が吐出される際、吐出孔334に対向して面する箇所が強く吐出され、陽極酸化処理により形成されたアルマイト皮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2を回転させる減速モータ21が装備されているため、ピストンWを回転させながら電解液を吐出させることによってアルマイト皮膜を均一に形成することができる。   Further, when the electrolytic solution is discharged, the portion facing the discharge hole 334 is strongly discharged, and the alumite film formed by the anodic oxidation treatment is held non-uniformly. Since the decelerating motor 21 for rotating the means 2 is equipped, the alumite film can be formed uniformly by discharging the electrolyte while rotating the piston W.

さらに、吐出孔334は、電極本体33の軸心に向かってオフセットして開口しており、電極本体33の軸心とピストンWの回転中心を同じに配置しているためピストンWの回転中心に対して電解液は吐出孔334からオフセットして吐出される。そのため吐出孔334に対向して面する箇所への電解液の当たり方が軽減され、より効率的にアルマイト皮膜を均一に形成することができる。   Further, the discharge hole 334 is offset and opened toward the axial center of the electrode main body 33, and the axial center of the electrode main body 33 and the rotation center of the piston W are arranged in the same position. On the other hand, the electrolyte is discharged from the discharge hole 334 with an offset. Therefore, the manner in which the electrolytic solution hits the portion facing the discharge hole 334 is reduced, and the alumite film can be uniformly formed more efficiently.

なお、本発明は、上記実施形態に限定されるものではなく、以下に示す態様に変更しても良い。   In addition, this invention is not limited to the said embodiment, You may change into the aspect shown below.

また、本発明の実施形態では集電リング61と、保持軸22と、ピストンWとで陽極を構成しているが、ピストンWに通電できるものであるならば保持手段を組み込まない構成も可能である。   In the embodiment of the present invention, the current collecting ring 61, the holding shaft 22, and the piston W constitute an anode. However, as long as the piston W can be energized, a configuration in which no holding means is incorporated is also possible. is there.

また、本実施例では電解液の流量を制御する流量計53、電解液を所定の温度に冷却する冷凍機512及び熱交換器513を組み入れた構成となっているが、実際に陽極酸化処理が行われる際、場合によっては組み入れない構成も可能である。   In this embodiment, the flow meter 53 for controlling the flow rate of the electrolytic solution, the refrigerator 512 for cooling the electrolytic solution to a predetermined temperature, and the heat exchanger 513 are incorporated. In some cases, a configuration that does not include it is possible.

また、本実施例では電極本体33の吐出孔334から電解液が吐出される際、吐出孔334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334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33の吐出孔334の均等性が保障される限り、吐出孔334は電極本体33の内周面に複数段列配置ができる。   In the present embodiment, when the electrolytic solution is discharged from the discharge hole 334 of the electrode body 33, the shape and size of the discharge hole 334 affects the effect of the anodizing treatment. When anodizing is performed, the discharge hole 334 may be elliptical or rectangular depending on circumstances. Further, as long as the uniformity of the discharge holes 334 of the electrode body 33 is ensured, the discharge holes 334 can be arranged in a plurality of stages on the inner peripheral surface of the electrode body 33.

また、本実施例では羽根板41は渦巻き曲線の一部を成す形状をしているが他の曲線形状、または直線形状にすることも可能である。   Further, in the present embodiment, the vane plate 41 has a shape forming a part of a spiral curve, but may be formed in another curved shape or a linear shape.

通電手段6は、電極部3の導体34と保持手段2との間に電圧を印加する手段であり、直流電源(図示せず)、電流計、電圧計、整流器(図示せず)集電リング61で構成され、従来公知のものを利用できる。なお、電流密度を制御できるものであれば本実施例の構成に限定するものではない。   The energizing means 6 is means for applying a voltage between the conductor 34 of the electrode section 3 and the holding means 2, and includes a DC power source (not shown), an ammeter, a voltmeter, and a rectifier (not shown) current collecting ring. It is comprised by 61 and a conventionally well-known thing can be utilized. Note that the configuration of this embodiment is not limited as long as the current density can be controlled.

1 :陽極酸化処理装置
2 :保持手段(第1電極部)
3 :電極部(第2電極部)
4 :羽根車部(電解液排出手段)
5 :電解液供給手段
6 :通電手段
7 :電解槽
8 :貯留部
41 :羽根板(誘導板)
45 :流路
311:第1円形凹部(電解液通路)
312:通路(電解液通路)
321:第2円形凹部(電解液通路)
326:通孔(電解液通路)
333:流入孔(電解液通路)
334:吐出孔(電解液吐出孔)
1: Anodizing apparatus 2: Holding means (first electrode part)
3: Electrode part (second electrode part)
4: Impeller part (electrolyte discharging means)
5: Electrolyte supply means 6: Energizing means 7: Electrolysis tank 8: Reservoir 41: Blade (guide plate)
45: Flow path 311: First circular recess (electrolyte passage)
312: passage (electrolyte passage)
321: Second circular recess (electrolyte passage)
326: Through hole (electrolyte passage)
333: Inflow hole (electrolyte passage)
334: Discharge hole (electrolyte discharge hole)

Claims (2)

側周面にリング状の溝部を有する金属製の被処理物に接触し電流を通電する第1電極部と、
前記被処理物と対向する電解液吐出孔と、前記吐出孔から吐出し前記被処理物の表面と接触した状態にある電解液を貯留する貯留部と、前記電解液吐出孔に電解液を供給する電解液通路と、を有する第2電極部と、
前記貯留部から過剰となった電解液を排出する電解液排出手段と、
前記電解液通路へ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電極部とに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、
前記電解液排出手段は、電解液を取り入れる取入口と、電解液を流す流路と、を有し、
前記流路は、前記電解液排出手段の回転中心から放射状に誘導板を備えており、
前記誘導板は、前記被処理物と一体に回転することを特徴とする陽極酸化処理装置。
A first electrode portion that contacts a metal workpiece having a ring-shaped groove on the side peripheral surface thereof and energizes a current;
An electrolyte solution discharge hole facing the object to be processed, a storage part for storing an electrolyte solution discharged from the discharge hole and in contact with the surface of the object to be processed, and supplying an electrolyte solution to the electrolyte solution discharge hole A second electrode portion having an electrolyte passage to perform,
An electrolyte discharging means for discharging the excess electrolyte from the reservoir;
An electrolyte supply means for supplying an electrolyte to the electrolyte passage;
Energization means for applying a voltage to the first electrode portion and the second electrode portion;
In an anodizing apparatus comprising :
The electrolyte discharge means has an inlet for taking in the electrolyte and a flow path for flowing the electrolyte,
The flow path is provided with a guide plate radially from the rotation center of the electrolyte discharging means,
The anodizing apparatus characterized in that the guide plate rotates integrally with the object to be processed .
前記電解液排出手段は、前記誘導板と、前記誘導板の上部に設けられるリング状の上部案内部と、前記誘導板の下部に設けられるリング状の下部案内部と、からなる、ことを特徴とする請求項1に記載の陽極酸化処理方法。 The electrolyte discharge means includes the guide plate, a ring-shaped upper guide portion provided on the upper portion of the guide plate, and a ring-shaped lower guide portion provided on the lower portion of the guide plate. The anodizing method according to claim 1.
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