JP4701072B2 - Method and apparatus for removing conductive metal oxide thin film - Google Patents

Method and apparatus for removing conductive metal oxide thin film Download PDF

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JP4701072B2
JP4701072B2 JP2005324991A JP2005324991A JP4701072B2 JP 4701072 B2 JP4701072 B2 JP 4701072B2 JP 2005324991 A JP2005324991 A JP 2005324991A JP 2005324991 A JP2005324991 A JP 2005324991A JP 4701072 B2 JP4701072 B2 JP 4701072B2
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thin film
metal oxide
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JP2007131894A (en
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博之 大工
鉄也 井上
健司 上川
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Hitachi Zosen Corp
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本発明は、例えばスパッタ蒸着などにより基材に形成された導電性金属酸化物薄膜を、再利用が可能なように除去する方法及びその方法を実施する装置に関するものである。   The present invention relates to a method for removing a conductive metal oxide thin film formed on a substrate by, for example, sputter deposition so that it can be reused, and an apparatus for carrying out the method.

例えばITO(インジウムとスズの酸化物で、透明導電性を有する膜)を形成した高機能ガラス基板は、光学的性能(透過率等)や機械的性能(平坦度等)に優れており、例えばフラットパネルディスプレイに用いられる。しかしながら、この高機能ガラス基板は高価であるため、その表面に形成するITOが品質管理基準を満足しない場合には、そのITOを除去して再利用することで、コストの低減を図っている。   For example, a high-performance glass substrate on which ITO (a film having transparent conductivity with an oxide of indium and tin) is excellent in optical performance (such as transmittance) and mechanical performance (such as flatness). Used for flat panel displays. However, since this high-functional glass substrate is expensive, when the ITO formed on the surface does not satisfy the quality control standard, the ITO is removed and reused to reduce the cost.

このITOなどの導電性金属酸化物薄膜を除去する方法として、機械的擦過により除去する方法や、化学エッチングにより除去する方法がある。このうち前者の方法は、図10に示すように、被加工物1の表面に形成した導電性金属酸化物薄膜1aを研摩ブラシ2により擦過することで除去するものである。   As a method of removing the conductive metal oxide thin film such as ITO, there are a method of removing by mechanical abrasion and a method of removing by chemical etching. Of these methods, the former method is to remove the conductive metal oxide thin film 1 a formed on the surface of the workpiece 1 by rubbing with a polishing brush 2 as shown in FIG. 10.

また、後者の方法は、図11に示すように、導電性金属酸化物薄膜1aを化学反応的に溶解させる化学液3に被加工物1を浸漬することで、その表面に形成した導電性金属酸化物薄膜1aを除去するものである(例えば特許文献1,2)。
特開平6−321581号公報 特開平9−86968号公報
In the latter method, as shown in FIG. 11, the conductive metal formed on the surface of the workpiece 1 is immersed in a chemical solution 3 that chemically dissolves the conductive metal oxide thin film 1a. The oxide thin film 1a is removed (for example, Patent Documents 1 and 2).
JP-A-6-321581 JP-A-9-86968

しかしながら、機械的擦過によって除去する方法は、研摩ブラシを擦りつけることから、被加工物の表面に擦過痕(疵)や応力変形を生じさせる場合がある。擦過痕が生じた場合、再利用ができなくなる。また、対象とする被加工物がフラットパネルディスプレイの場合、ガラス基板のガラス厚みが0.5mm程度であるため、接触方式の機械的擦過では破損する可能性がある。従って、微妙なブラシの圧力調整が必要で、完全に剥離するためには長時間を要する。   However, since the method of removing by mechanical rubbing rubs the polishing brush, there are cases where rubbing marks (wrinkles) and stress deformation occur on the surface of the workpiece. When scratch marks are generated, it cannot be reused. Moreover, when the object to be processed is a flat panel display, the glass thickness of the glass substrate is about 0.5 mm. Therefore, delicate pressure adjustment of the brush is necessary, and it takes a long time to completely peel off.

一方、化学エッチングによって除去する方法は、強酸や強アルカリの化学液を使用するので、基板表面に化学的応力が発生し、基板表面に変質層を生じさせる場合がある。また、取扱いに十分な注意を払う必要があり、作業性が悪くなるばかりでなく、使用後の電解液を廃液処理する必要がある。また、希少金属の回収には、別途抽出作業を必要とするために非常に不経済である。   On the other hand, the method of removing by chemical etching uses a strong acid or strong alkali chemical solution, so that chemical stress is generated on the surface of the substrate and an altered layer may be formed on the surface of the substrate. In addition, it is necessary to pay sufficient attention to handling, not only the workability is deteriorated, but also the electrolytic solution after use needs to be treated as a waste solution. Also, the collection of rare metals is very uneconomical because it requires a separate extraction operation.

本発明が解決しようとする問題点は、機械的擦過による方法では、擦過痕や応力変形が生じて基材を再利用できなくなり、また、ブラシの微妙な圧力調整が必要で完全剥離に長時間を要するという点、化学エッチングによる方法では、基板表面に変質層を生じさせる場合があり、また作業性が悪くなるばかりか、使用後の電解液を廃液処理する必要があり、しかも、希少金属の回収に別途抽出作業が必要で、不経済であるという点である。   The problems to be solved by the present invention are that mechanical scratching causes scratch marks and stress deformation, making it impossible to reuse the substrate, and delicate pressure adjustment of the brush is necessary, and complete peeling takes a long time. In the method using chemical etching, a deteriorated layer may be formed on the surface of the substrate, and workability is deteriorated. In addition, it is necessary to dispose the used electrolytic solution as a waste liquid. This requires that a separate extraction operation is required for collection, which is uneconomical.

本発明の導電性金属酸化物薄膜の除去方法は、
基材に擦過痕や応力変形などを残さず、かつ、強酸や強アルカリの化学液を使用しないで、基材の導電性金属酸化物薄膜を基材の端部まで、僅かな残留膜もなく、効率良く除去するために、
基材の表面に形成された導電性金属酸化物薄膜に対向すべく、正電極と負電極を交互に複数対配置した後、
これらの正電極、負電極と前記導電性金属酸化物薄膜間に電解液を介在させた状態で、前記両電極に電圧を印加し、前記の正電極及び負電極を、前記導電性金属酸化物薄膜との相対位置を変化すべく、隣接する電極方向に移動させることで、前記基材表面の導電性金属酸化物薄膜を還元反応により除去することを最も主要な特徴としている。
The method for removing the conductive metal oxide thin film of the present invention comprises:
Without leaving scratch marks or stress deformation on the base material, and without using a strong acid or strong alkali chemical solution, the conductive metal oxide thin film of the base material has no residual film up to the edge of the base material. In order to remove efficiently,
In order to face the conductive metal oxide thin film formed on the surface of the substrate, a plurality of pairs of positive and negative electrodes are alternately arranged,
A voltage is applied to both of the positive electrode and the negative electrode while the electrolyte is interposed between the positive electrode, the negative electrode and the conductive metal oxide thin film , and the positive electrode and the negative electrode are connected to the conductive metal oxide. in order to change the relative position of the thin film, in Rukoto move to the adjacent electrode direction, and the most important feature be removed by a reduction reaction a conductive metal oxide thin film of the substrate surface.

この本発明の導電性金属酸化物薄膜の除去方法では、導電性金属酸化物薄膜に対向すべく、正電極と負電極を交互に複数対配置することにより、基材の表面に形成された導電性金属酸化物薄膜を広範囲に除去することができる。   In this method for removing a conductive metal oxide thin film according to the present invention, a plurality of pairs of positive and negative electrodes are alternately arranged to face the conductive metal oxide thin film, thereby forming a conductive film formed on the surface of the substrate. The conductive metal oxide thin film can be removed over a wide range.

本発明の導電性金属酸化物薄膜の除去方法では、正電極及び負電極を、導電性金属酸化物薄膜との相対位置を変化すべく、隣接する電極方向に移動させるので、少しの移動により、電極配置方向の導電性金属酸化物薄膜を一度に除去できる。 In removing method of the conductive metal oxide thin film of the present invention, the positive and negative electrodes, in order to change the relative position between the conductive metal oxide thin film, Runode move to the adjacent electrode direction by slightly moving The conductive metal oxide thin film in the electrode arrangement direction can be removed at a time.

前記本発明の導電性金属酸化物薄膜の除去方法においては、抵抗率が103Ω・cmから106Ω・cmの電解液を使用することで、基材表面に形成された導電性金属酸化物薄膜を効率良く除去することが可能になる。 In the method for removing a conductive metal oxide thin film of the present invention, the conductive metal oxide formed on the surface of the substrate is used by using an electrolyte having a resistivity of 10 3 Ω · cm to 10 6 Ω · cm. It is possible to efficiently remove the physical thin film.

本発明の導電性金属酸化物薄膜の除去装置は、
基材の表面に形成された導電性金属酸化物薄膜に対向すべく、交互に複数対配置された正電極及び負電極と、
これら正電極、負電極と前記基材の表面に形成された導電性金属酸化物薄膜間に電解液を供給する手段、或いは、前記の正電極、負電極と基材を電解液内に浸漬すべく電解液を貯留する電解液槽と、
1) これらの正電極と負電極に電圧を印加する電源を備え、
前記の交互に複数対配置した正電極及び負電極は、前記導電性金属酸化物薄膜に対向すべく配置された平面状の負電極を複数列の正電極が貫通するように配置したことを、
或いは、
2) これらの正電極と負電極に電圧を印加する電源と、
前記の正電極と負電極を、前記導電性金属酸化物薄膜との相対位置を変化すべく、隣接する電極方向に移動させる移動装置を備えたものであることを、
最も主要な特徴としている
The apparatus for removing a conductive metal oxide thin film of the present invention comprises:
A plurality of positive and negative electrodes alternately arranged to face the conductive metal oxide thin film formed on the surface of the substrate;
Means for supplying an electrolytic solution between the positive electrode, the negative electrode and the conductive metal oxide thin film formed on the surface of the substrate, or the positive electrode, the negative electrode and the substrate are immersed in the electrolytic solution An electrolyte tank for storing the electrolyte as much as possible,
1) Preparations to give a power source for applying a voltage to the positive and negative electrodes,
The plurality of alternately arranged positive electrodes and negative electrodes are arranged such that a plurality of rows of positive electrodes pass through a planar negative electrode arranged to face the conductive metal oxide thin film.
Or
2) a power supply that applies voltage to these positive and negative electrodes;
It is provided with a moving device that moves the positive electrode and the negative electrode in the direction of the adjacent electrode in order to change the relative position of the conductive metal oxide thin film,
The most important feature .

後者の本発明の導電性金属酸化物薄膜の除去装置では、前記の交互に複数対配置した正電極及び負電極は、線状又は板状のものを1列に配置したもの等が採用される。 The latter in apparatus for removing conductive metal oxide thin film of the present invention, the positive and negative electrodes in which a plurality pairs arranged alternately Said, etc. were also placed as linear or plate-like in one row is adopted The

状又は板状のものを1列に配置した正電極及び負電極を備えた後者の本発明の導電性金属酸化物薄膜の除去装置において、前記導電性金属酸化物薄膜に対向する正電極及び負電極の前記線状又は板状の方向が、隣接する電極方向に対して斜めとなるように配置すれば、より広範囲の導電性金属酸化物薄膜を除去することができる。 In the latter apparatus for removing a conductive metal oxide thin film according to the present invention, comprising a positive electrode and a negative electrode in which linear or plate-like ones are arranged in a row, a positive electrode facing the conductive metal oxide thin film, If the linear or plate-like direction of the negative electrode is disposed so as to be oblique with respect to the adjacent electrode direction , a wider range of conductive metal oxide thin film can be removed.

そして、この後者の本発明の導電性金属酸化物薄膜の除去装置において、正電極と負電極を、導電性金属酸化物薄膜との相対位置を変化すべく、隣接する電極方向に移動させる移動装置を備えさせた場合には、少しの移動により、電極配置方向の導電性金属酸化物薄膜を一度に除去できるようになる。 Also in the apparatus for removing conductive metal oxide thin film of the latter invention of this, the positive electrode and the negative electrode, in order to change the relative position between the conductive metal oxide thin film is moved to the adjacent electrode direction When the moving device is provided, the conductive metal oxide thin film in the electrode arrangement direction can be removed at a time by a slight movement.

本発明では、正電極と負電極を交互に複数対配置するので、一度に広範囲にわたって導電性金属酸化物薄膜の除去が行える。そして、その際、電解溶出で付着力を弱めた後に、基材に形成された導電性金属を除去すれば、基材に疵や応力変形などを残すことなく、導電性金属酸化物薄膜を基材端部まで効率良く除去でき、半導体分野で用いられる高価な機能性ガラス基板などの再生利用が可能になる。また、強酸や強アルカリの化学液を使用しないので、環境負荷も低減でき、基材を始めとする希少金属などの資源サイクルも可能になって、経済的にも有利である。   In the present invention, since a plurality of pairs of positive electrodes and negative electrodes are alternately arranged, the conductive metal oxide thin film can be removed over a wide range at a time. At that time, if the conductive metal formed on the substrate is removed after weakening the adhesive force by electrolytic elution, the conductive metal oxide thin film can be formed without leaving wrinkles or stress deformation on the substrate. It can be efficiently removed to the end of the material, and it becomes possible to recycle an expensive functional glass substrate used in the semiconductor field. Further, since no strong acid or strong alkali chemical solution is used, the environmental load can be reduced, and resource cycles such as rare metals such as base materials can be realized, which is economically advantageous.

以下、本発明方法の基本原理を、図1を用いて説明した後、本発明を実施するための最良の形態を図2〜図9を用いて詳細に説明する。
本発明は、基材への疵や応力変形などを残さない加工法で、かつ、強酸や強アルカリを使用しない導電性金属酸化物薄膜の除去方法である。
Hereinafter, the basic principle of the method of the present invention will be described with reference to FIG. 1, and then the best mode for carrying out the present invention will be described in detail with reference to FIGS.
The present invention is a processing method that does not leave wrinkles or stress deformation on a substrate, and a method for removing a conductive metal oxide thin film that does not use strong acid or strong alkali.

つまり、図1のように、表面に導電性金属酸化物薄膜12を形成した絶縁物や導電物などの基材11と、その上方に所定の間隔を存して配置した正電極13及び負電極14を、電解液槽内の電解液15に浸漬配置し、電源16から直流電圧或いはパルス電圧を印加するのである。   That is, as shown in FIG. 1, a base material 11 such as an insulator or a conductive material having a conductive metal oxide thin film 12 formed on the surface thereof, and a positive electrode 13 and a negative electrode disposed above the base material 11 with a predetermined interval therebetween. 14 is immersed in the electrolytic solution 15 in the electrolytic solution tank, and a DC voltage or a pulse voltage is applied from the power source 16.

このようにすることで、電源16(+)−正電極13−電解液15−導電性金属酸化物薄膜12−電解液15−負電極14−電源16(−)の閉回路が形成され、正電極13近傍の導電性金属酸化物薄膜12の表面からH2の微細気泡が発生する。 In this way, a closed circuit of the power source 16 (+)-positive electrode 13-electrolytic solution 15-conductive metal oxide thin film 12-electrolytic solution 15-negative electrode 14-power source 16 (-) is formed. H 2 fine bubbles are generated from the surface of the conductive metal oxide thin film 12 in the vicinity of the electrode 13.

このとき、正電極13近傍の導電性金属酸化物薄膜12の表面に発生するH2が還元剤となり、導電性金属酸化物薄膜12中のO2を取り除く作用が生じる。さらに、このH2の発生は導電性金属酸化物薄膜12の界面で生じることから効率の良い還元反応が生じる。 At this time, H 2 generated on the surface of the conductive metal oxide thin film 12 in the vicinity of the positive electrode 13 serves as a reducing agent, and an action of removing O 2 in the conductive metal oxide thin film 12 occurs. Furthermore, since the generation of H 2 occurs at the interface of the conductive metal oxide thin film 12, an efficient reduction reaction occurs.

2による結合が無くなった導電性金属酸化物薄膜12は金属元素だけとなり、基材11の表面に結合力が弱まった状態で存在するようになる。基材11との結合が弱まった導電性金属12aは、弱い応力で擦過する例えば回転スポンジ体などの柔軟性体によって基材11から確実に除去される。 The conductive metal oxide thin film 12 that is no longer bonded by O 2 contains only a metal element, and exists on the surface of the base material 11 in a state where the bonding force is weakened. The conductive metal 12a whose bond with the base material 11 has been weakened is reliably removed from the base material 11 by a flexible material such as a rotating sponge body that is rubbed with a weak stress.

しかしながら、図1のような電極配置では、最終端部になると、導電性金属酸化物薄膜12と負電極14との距離Dが長くなり、導電性金属酸化物薄膜12に流れる電流量が電解液15中に比べて減少し、電流効率が悪くなる。   However, in the electrode arrangement as shown in FIG. 1, at the final end, the distance D between the conductive metal oxide thin film 12 and the negative electrode 14 becomes long, and the amount of current flowing through the conductive metal oxide thin film 12 is reduced by the electrolyte. 15 and the current efficiency is deteriorated.

そこで、本発明では、例えば電解液槽内の電解液15に浸漬する正電極13と負電極14を、基材11の表面に形成された導電性金属酸化物薄膜12に対向すべく、図2や図3に示したように、交互に複数対配置するのである。   Therefore, in the present invention, for example, the positive electrode 13 and the negative electrode 14 immersed in the electrolytic solution 15 in the electrolytic solution tank are opposed to the conductive metal oxide thin film 12 formed on the surface of the substrate 11 as shown in FIG. As shown in FIG. 3, a plurality of pairs are alternately arranged.

例えば図2は、棒やワイヤ等の線状、或いは板状の電極を1列に配置した例である。また、図3は、例えば網目状に形成した負電極14の、網目内全てを正電極13が貫通するように配置したものである。この場合、網目状の負電極14は、基材11の表面に形成された導電性金属酸化物薄膜12に対向すべく配置され、正電極13と負電極14は絶縁体17を介して配置されている。なお、図2中の20は基板を示す。   For example, FIG. 2 shows an example in which linear or plate-like electrodes such as rods and wires are arranged in a line. FIG. 3 shows the arrangement of the negative electrode 14 formed in a mesh shape, for example, so that the positive electrode 13 penetrates the entire mesh. In this case, the net-like negative electrode 14 is disposed so as to face the conductive metal oxide thin film 12 formed on the surface of the substrate 11, and the positive electrode 13 and the negative electrode 14 are disposed via the insulator 17. ing. Note that reference numeral 20 in FIG. 2 denotes a substrate.

このうち、図2及び図3の構成の場合は、例えば図4のように、正電極13の下流側に柔軟性のある機械的擦過機構、例えば回転スポンジ体18を配置し、基材11を正電極13と隣接する正電極13の距離分だけ水平移動可能に構成すれば、効率良く広範囲にわたって導電性金属酸化物薄膜12を除去できる。   Among these, in the case of the configuration of FIGS. 2 and 3, for example, as shown in FIG. When configured to be horizontally movable by the distance between the positive electrode 13 and the adjacent positive electrode 13, the conductive metal oxide thin film 12 can be efficiently removed over a wide range.

そして、その際、前記導電性金属酸化物薄膜12に対向する前記1列に配置した正電極13及び負電極14の前記線状又は板状の方向が、図5に示すように、隣接する電極方向に対して斜めとなるように配置すれば、例えば紙面上方の第1電極対では第1領域E1を、また次の第2電極対では第2領域E2…というように、導電性金属酸化物薄膜12をより広範囲にわたって除去できる。加えて、基材11の移動によって導電性金属酸化物薄膜12をより広範囲にわたって還元できるので、電極13,14の長さLを短くすることができる。また、基材11の水平移動が不要となる。 At that time, the linear or plate-like directions of the positive electrode 13 and the negative electrode 14 arranged in the one row facing the conductive metal oxide thin film 12 are adjacent to each other as shown in FIG. When arranged so as to be inclined with respect to the direction , for example, the first region E1 in the first electrode pair above the paper surface, the second region E2 in the next second electrode pair, etc., the conductive metal oxide. The thin film 12 can be removed over a wider range. In addition, since the conductive metal oxide thin film 12 can be reduced over a wider range by the movement of the base material 11, the length L of the electrodes 13, 14 can be shortened. Moreover, the horizontal movement of the base material 11 becomes unnecessary.

但し、図5のように、電極13,14を斜めに設ける場合は、その電極角度をθ、正電極13の間隔をX、長さをLとした場合、X/L≦sinθの関係となるようにしなければならない。これはX/L>sinθの関係になると、第1領域E1と第2領域E2との間に還元反応が生じない領域ができるためである。   However, when the electrodes 13 and 14 are provided obliquely as shown in FIG. 5, when the electrode angle is θ, the interval between the positive electrodes 13 is X, and the length is L, the relationship is X / L ≦ sin θ. Must do so. This is because when X / L> sin θ, the region where the reduction reaction does not occur between the first region E1 and the second region E2.

このような、電極配置では、正電極13と負電極14を交互に複数対配置しているので、負電極14が導電性金属酸化物薄膜12から離れるのは、基材11の隅部分だけとなって、導電性金属酸化物薄膜12の残留部分を極力少なくできる。   In such an electrode arrangement, since a plurality of pairs of positive electrodes 13 and negative electrodes 14 are alternately arranged, the negative electrodes 14 are separated from the conductive metal oxide thin film 12 only at the corners of the substrate 11. Thus, the remaining portion of the conductive metal oxide thin film 12 can be reduced as much as possible.

ところで、導電性酸化物薄膜12が還元反応される速度は、主に印加電圧と両電極13,14の間隔によって決まり、印加電圧/電極間隔の大きいほうが還元反応速度は速くなる。電極間隔が短く、電圧が高い方が、回路を流れる電流が大きくなって、Hの発生量が増加するためである。 By the way, the rate at which the conductive oxide thin film 12 undergoes the reduction reaction is mainly determined by the applied voltage and the distance between the electrodes 13 and 14. The larger the applied voltage / electrode distance, the faster the reduction reaction rate. This is because when the electrode interval is shorter and the voltage is higher, the current flowing through the circuit becomes larger and the amount of H + generated increases.

しかしながら、還元反応速度を速めるために印加電圧を大きくすると、高電圧の電源が必要となって、効率が悪くなる。加えて、印加電圧/電極間隔を大きくしすぎると、電極間で絶縁破壊を生じ、放電を発生して基材11を損傷させる恐れがある。   However, if the applied voltage is increased in order to increase the reduction reaction rate, a high-voltage power source is required, resulting in poor efficiency. In addition, if the applied voltage / electrode interval is too large, dielectric breakdown may occur between the electrodes, and a discharge may be generated to damage the substrate 11.

そこで、本発明では、正電極13と負電極14を交互に複数対配置することで、高い電圧を印加しなくても、電極下部に相当する大面積を一挙に還元反応ができるようにし、処理速度を向上させた。   Therefore, in the present invention, a plurality of pairs of the positive electrode 13 and the negative electrode 14 are alternately arranged so that a large area corresponding to the lower portion of the electrode can be reduced at a time without applying a high voltage. Increased speed.

また、図6は、図3の構成の電極を採用し、電解液15の上方に基材11を引き上げるように構成したものである。このような構成では、基材11の引き上げ位置に回転スポンジ体18を配置すれば、小さな装置設置面積で、効率良く導電性金属酸化物薄膜12を除去できるようになる。   Further, FIG. 6 employs an electrode having the configuration shown in FIG. 3 so that the substrate 11 is pulled up above the electrolyte solution 15. In such a configuration, the conductive metal oxide thin film 12 can be efficiently removed with a small apparatus installation area by disposing the rotating sponge body 18 at the lifting position of the substrate 11.

加えて、このような電極構成では、網目状に形成した負電極14の、網目内全てを正電極13が貫通しており、1つの正電極13で除去する範囲は1つの網目内だけとなる。従って、短い正電極13と負電極14間に低電圧を印加しただけでも、網目状の負電極14全体を一挙に還元反応ができ、処理速度が向上する。   In addition, in such an electrode configuration, the positive electrode 13 penetrates all the inside of the mesh of the negative electrode 14 formed in a mesh shape, and the range to be removed by one positive electrode 13 is only within one mesh. . Therefore, even if a low voltage is applied between the short positive electrode 13 and the negative electrode 14, the entire net-like negative electrode 14 can be reduced at once and the processing speed is improved.

また、網目内を貫通する正電極13の周囲には電解集中が生じ、それによって正電極13の先端には電流が集中して電流密度が高くなるので、その部分でのHの発生密度が増加し、低電圧の印加でも効率の良い還元反応を生じさせることができる。 Also, electrolytic concentration occurs around the positive electrode 13 penetrating through the mesh, thereby concentrating current at the tip of the positive electrode 13 and increasing the current density. Therefore, the generation density of H + at that portion increases. The efficiency of the reduction reaction can be increased even when a low voltage is applied.

この図3の構成の電極を、図7のように、図6に示した電極の背面側にも設けることで、1組の電極で2枚の基材11の処理が可能になる。   3 is provided also on the back surface side of the electrode shown in FIG. 6, as shown in FIG. 7, the two substrates 11 can be processed with one set of electrodes.

また、図3の構成の電極を採用する場合、図6のように電解液17に浸漬する構成に代えて、図8のように正電極13の内部を通って基材11の導電性金属酸化物薄膜12に向けて電解液15を噴射することで、O2が無くなり基材11との結合力が弱まった導電性金属酸化物薄膜12を除去するようにしても良い。 When the electrode having the configuration shown in FIG. 3 is employed, the conductive metal oxide of the substrate 11 passes through the inside of the positive electrode 13 as shown in FIG. 8 instead of being immersed in the electrolyte solution 17 as shown in FIG. By injecting the electrolyte solution 15 toward the physical thin film 12, the conductive metal oxide thin film 12 whose O 2 is eliminated and the bonding force with the base material 11 is weakened may be removed.

上述の本発明において、導電性金属酸化物薄膜12との相対位置を変化すべく、正電極13と負電極14を隣接する電極方向に移動(正電極13と隣接する正電極13の距離分)させる移動装置を設け、電極13,14を例えば図6(a)の白抜き矢印方向に移動させながら基材11を水平移動或いは引き上げれば、導電性金属酸化物薄膜12の全面を効率良く除去できる。   In the above-described present invention, the positive electrode 13 and the negative electrode 14 are moved in the direction of the adjacent electrodes in order to change the relative position with the conductive metal oxide thin film 12 (the distance between the positive electrode 13 and the adjacent positive electrode 13). If the substrate 11 is moved horizontally or pulled up while moving the electrodes 13, 14 in the direction of the white arrow in FIG. 6A, for example, the entire surface of the conductive metal oxide thin film 12 is efficiently removed. it can.

以上の説明のように、本発明は、一般に行われている、被加工物に正電圧を印加する電解溶出除去反応ではなく、被加工物に負の電圧を印加する特徴的な加工法である。
なお、ここでの電解反応は導電性金属酸化物薄膜界面のごく微量な領域にH2の発生を生じさせるもので良いため、電流はほとんど必要としない。
As described above, the present invention is a characteristic processing method for applying a negative voltage to a workpiece, not a general electrolytic elution removal reaction for applying a positive voltage to the workpiece, as described above. .
Note that since the electrolytic reaction here may generate H 2 in a very small region at the interface of the conductive metal oxide thin film, little current is required.

従って、使用する電解液15は、一般に用いられる中性塩溶液でも利用可能であるが、正電極13、負電極14ともに基材11とは非接触の場合は、好ましくは、前述のように抵抗率が103Ω・cmから106Ω・cm、より好ましくは10Ω・cmから10Ω・cmのものが良い。 Accordingly, the electrolytic solution 15 to be used can be used as a neutral salt solution which is generally used. However, when both the positive electrode 13 and the negative electrode 14 are not in contact with the base material 11, it is preferable to use a resistance as described above. The rate is from 10 3 Ω · cm to 10 6 Ω · cm, more preferably from 10 4 Ω · cm to 10 5 Ω · cm.

本発明では、正電極13、負電極14ともに基材11とは非接触の場合、抵抗率が103Ω・cm未満の導電性の高い電解液15では、両電極13,14間に印加された電圧が、導電性金属酸化物薄膜12を通さず、前記両電極13,14間で電解液15を通して導通状態となるため、導電性金属酸化物薄膜12の除去効率が低下するからである。また、抵抗率が106Ω・cmを超えると高電圧を印加する必要があり、経済上好ましくないからである。 In the present invention, when both the positive electrode 13 and the negative electrode 14 are not in contact with the base material 11, a highly conductive electrolyte 15 having a resistivity of less than 10 3 Ω · cm is applied between the electrodes 13 and 14. This is because, since the voltage does not pass through the conductive metal oxide thin film 12 and becomes conductive through the electrolytic solution 15 between the electrodes 13 and 14, the removal efficiency of the conductive metal oxide thin film 12 decreases. Further, if the resistivity exceeds 10 6 Ω · cm, it is necessary to apply a high voltage, which is economically undesirable.

このように本発明では、抵抗率の比較的高い電解液15が適していることから、従来、電解液15としては好ましくなかった、水道水や河川水等を用いることができ、経済性および安全性の面においても優れている。   Thus, in the present invention, since the electrolytic solution 15 having a relatively high resistivity is suitable, tap water, river water, and the like, which are not preferable as the electrolytic solution 15 conventionally, can be used. Also excellent in terms of sex.

本発明は、前述の例に限るものではなく、各請求項に記載の技術的思想の範囲内において、適宜実施の形態を変更しても良いことは言うまでもない。   The present invention is not limited to the above-described examples, and it goes without saying that the embodiments may be appropriately changed within the scope of the technical idea described in each claim.

例えば平面状の負電極14を複数列の正電極13が貫通する構成は、図3のように網目状に形成した負電極14に限らず、絶縁体17の表面にめっきを施してパターン化した負電極14を形成しても良い。   For example, the configuration in which a plurality of rows of positive electrodes 13 pass through the planar negative electrode 14 is not limited to the negative electrode 14 formed in a mesh shape as shown in FIG. 3, and is patterned by plating the surface of the insulator 17. The negative electrode 14 may be formed.

このような負電極14を用いた場合、基材11上の所望の位置の導電性金属酸化物薄膜12のみを除去することができる。また、基材11を移動させれば、電極13,14を移動させなくても、導電性金属酸化物薄膜12の全面を除去できるようになる。   When such a negative electrode 14 is used, only the conductive metal oxide thin film 12 at a desired position on the substrate 11 can be removed. Further, if the substrate 11 is moved, the entire surface of the conductive metal oxide thin film 12 can be removed without moving the electrodes 13 and 14.

また、図2のように、線状或いは板状の電極13,14を1列に配置したものでは、図9のように、両電極13,14が電解質膜19を介して接触するように構成しても良い。この場合、電解質膜19の採用により、正電極13から発生するO2による還元反応の低下を防ぎ、安定して導電性金属酸化物薄膜を除去できるようになる。 In addition, in the case where the linear or plate-like electrodes 13 and 14 are arranged in a row as shown in FIG. 2, the electrodes 13 and 14 are in contact with each other through the electrolyte membrane 19 as shown in FIG. You may do it. In this case, the use of the electrolyte membrane 19 prevents the reduction of the reduction reaction due to O 2 generated from the positive electrode 13 and enables the conductive metal oxide thin film to be removed stably.

この手法は平面状の負電極14を複数列の正電極13が貫通する構成でも使用できる。この場合、導電性金属酸化物薄膜12の全面を除去するには、両電極13,14の移動が必要であるため、平面状の電極を正電極13、この平面状の電極を貫通する電極を負電極14としても良い。   This method can also be used in a configuration in which a plurality of rows of positive electrodes 13 pass through the planar negative electrode 14. In this case, in order to remove the entire surface of the conductive metal oxide thin film 12, it is necessary to move both electrodes 13 and 14. Therefore, the planar electrode is the positive electrode 13, and the electrode penetrating the planar electrode is formed. The negative electrode 14 may be used.

本発明の基本原理を説明する図である。It is a figure explaining the basic principle of this invention. 本発明装置を構成する電極の第1の例を説明する概略図で、棒やワイヤ等の線状、或いは板状の電極を1列に配置した例を示した図である。It is the schematic explaining the 1st example of the electrode which comprises this invention apparatus, and is the figure which showed the example which has arrange | positioned linear or plate-like electrodes, such as a rod and a wire, in 1 row. 本発明装置を構成する電極の第2の例を説明する概略図で、網目状に形成した負電極の、網目内全てを正電極が貫通するように配置した例を示した図である。It is the schematic explaining the 2nd example of the electrode which comprises this invention apparatus, and is the figure which showed the example arrange | positioned so that the positive electrode may penetrate all the insides of the net | network of the negative electrode formed in mesh shape. 図2の電極を用いた本発明装置の概略説明図で、上方から見た図である。It is the schematic explanatory drawing of this invention apparatus using the electrode of FIG. 2, and is the figure seen from upper direction. 図4において電極を斜めに配置した場合の本発明装置の概略説明図である。It is a schematic explanatory drawing of this invention apparatus at the time of arrange | positioning an electrode diagonally in FIG. 図3の電極を用いた本発明装置の概略説明図で、(a)は斜視図、(b)は要部拡大図である。It is a schematic explanatory drawing of this invention apparatus using the electrode of FIG. 3, (a) is a perspective view, (b) is a principal part enlarged view. 図3の電極を背面側にも設けた構成の、図6に示した本発明装置の概略説明図である。It is a schematic explanatory drawing of the apparatus of this invention shown in FIG. 6 of the structure which provided the electrode of FIG. 3 also in the back side. 正電極の内部を通って基材の導電性金属酸化物薄膜に向けて電解液を噴射する図6の本発明装置の要部拡大図である。It is a principal part enlarged view of the apparatus of this invention of FIG. 6 which injects electrolyte solution toward the electroconductive metal oxide thin film of a base material through the inside of a positive electrode. 両電極が電解質膜を介して接触するように構成した場合の例を示した図である。It is the figure which showed the example at the time of comprising so that both electrodes may contact via an electrolyte membrane. 機械的擦過により金属薄膜を除去する方法について説明する図である。It is a figure explaining the method of removing a metal thin film by mechanical abrasion. 化学エッチングにより金属薄膜を除去する方法について説明する図である。It is a figure explaining the method of removing a metal thin film by chemical etching.

符号の説明Explanation of symbols

11 基材
12 導電性金属酸化物薄膜
12a 導電性金属
13 正電極
14 負電極
15 電解液
16 電源
18 回転スポンジ体
DESCRIPTION OF SYMBOLS 11 Base material 12 Conductive metal oxide thin film 12a Conductive metal 13 Positive electrode 14 Negative electrode 15 Electrolytic solution 16 Power supply 18 Rotating sponge body

Claims (7)

基材の表面に形成された導電性金属酸化物薄膜に対向すべく、正電極と負電極を交互に複数対配置した後、
これらの正電極、負電極と前記導電性金属酸化物薄膜間に電解液を介在させた状態で、前記両電極に電圧を印加し、前記の正電極及び負電極を、前記導電性金属酸化物薄膜との相対位置を変化すべく、隣接する電極方向に移動させることで、前記基材表面の導電性金属酸化物薄膜を還元反応により除去することを特徴とする導電性金属酸化物薄膜の除去方法。
In order to face the conductive metal oxide thin film formed on the surface of the substrate, a plurality of pairs of positive and negative electrodes are alternately arranged,
A voltage is applied to both of the positive electrode and the negative electrode while the electrolyte is interposed between the positive electrode, the negative electrode and the conductive metal oxide thin film , and the positive electrode and the negative electrode are connected to the conductive metal oxide. in order to change the relative position of the thin film, in Rukoto move to the adjacent electrode direction, the conductive metal oxide thin film, and removing by a reduction reaction a conductive metal oxide thin film of the substrate surface Removal method.
前記電解液は、抵抗率が10 3 Ω・cmから10 6 Ω・cmのものを使用することを特徴とする請求項1に記載の導電性金属酸化物薄膜の除去方法。 The electrolyte, a method for removing the electrically conductive metal oxide thin film according to claim 1, resistivity, characterized in that you use those from 10 3 Ω · cm of 10 6 Ω · cm. 基材の表面に形成された導電性金属酸化物薄膜に対向すべく、交互に複数対配置された正電極及び負電極と、
これら正電極、負電極と前記基材の表面に形成された導電性金属酸化物薄膜間に電解液を供給する手段、或いは、前記の正電極、負電極と基材を電解液内に浸漬すべく電解液を貯留する電解液槽と、
これらの正電極と負電極に電圧を印加する電源を備え、
前記の交互に複数対配置した正電極及び負電極は、前記導電性金属酸化物薄膜に対向すべく配置された平面状の負電極を複数列の正電極が貫通するように配置したものであることを特徴とする導電性金属酸化物薄膜の除去装置
A plurality of positive and negative electrodes alternately arranged to face the conductive metal oxide thin film formed on the surface of the substrate;
Means for supplying an electrolytic solution between the positive electrode, the negative electrode and the conductive metal oxide thin film formed on the surface of the substrate, or the positive electrode, the negative electrode and the substrate are immersed in the electrolytic solution An electrolyte tank for storing the electrolyte as much as possible,
It has a power supply that applies voltage to these positive and negative electrodes,
The positive electrode and the negative electrode arranged alternately in pairs are arranged so that a plurality of rows of positive electrodes pass through the planar negative electrode arranged to face the conductive metal oxide thin film. conductive you wherein Rukoto metal oxide thin film removal device.
材の表面に形成された導電性金属酸化物薄膜に対向すべく、交互に複数対配置された正電極及び負電極と、
これら正電極、負電極と前記基材の表面に形成された導電性金属酸化物薄膜間に電解液を供給する手段、或いは、前記の正電極、負電極と基材を電解液内に浸漬すべく電解液を貯留する電解液槽と、
これらの正電極と負電極に電圧を印加する電源と、
前記の正電極と負電極を、前記導電性金属酸化物薄膜との相対位置を変化すべく、隣接する電極方向に移動させる移動装置を備えたものであることを特徴とする導電性金属酸化物薄膜の除去装置。
A plurality of positive and negative electrodes alternately arranged to face the conductive metal oxide thin film formed on the surface of the substrate;
Means for supplying an electrolytic solution between the positive electrode, the negative electrode and the conductive metal oxide thin film formed on the surface of the substrate, or the positive electrode, the negative electrode and the substrate are immersed in the electrolytic solution An electrolyte tank for storing the electrolyte as much as possible,
A power supply for applying a voltage to these positive and negative electrodes ;
A conductive metal oxide comprising a moving device for moving the positive electrode and the negative electrode in the direction of an adjacent electrode so as to change a relative position of the conductive metal oxide thin film . Thin film removal device.
前記の交互に複数対配置した正電極及び負電極は、線状又は板状のものを1列に配置したものであることを特徴とする請求項4に記載の導電性金属酸化物薄膜の除去装置。   The removal of the conductive metal oxide thin film according to claim 4, wherein the plurality of alternately arranged positive electrodes and negative electrodes are linear or plate-like ones arranged in a line. apparatus. 前記線状又は板状のものを1列に配置した正電極及び負電極は、前記導電性金属酸化物薄膜に対向する正電極及び負電極の前記線状又は板状の方向が、隣接する電極方向に対して斜めに配置したものであることを特徴とする請求項5に記載の導電性金属酸化物薄膜の除去装置。 The positive electrode and the negative electrode in which the linear or plate-like ones are arranged in a line are electrodes in which the linear or plate-like directions of the positive and negative electrodes facing the conductive metal oxide thin film are adjacent to each other. The apparatus for removing a conductive metal oxide thin film according to claim 5, wherein the apparatus is disposed obliquely with respect to the direction . 前記の正電極と負電極を、前記導電性金属酸化物薄膜との相対位置を変化すべく、隣接する電極方向に移動させる移動装置を備えたことを特徴とする請求項に記載の導電性金属酸化物薄膜の除去装置。 The electroconductive material according to claim 3 , further comprising a moving device that moves the positive electrode and the negative electrode in the direction of an adjacent electrode so as to change a relative position of the electroconductive metal oxide thin film . Metal oxide thin film removal device.
JP2005324991A 2005-11-09 2005-11-09 Method and apparatus for removing conductive metal oxide thin film Expired - Fee Related JP4701072B2 (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5175638A (en) * 1974-12-26 1976-06-30 Stanley Electric Co Ltd MUSETSUZOKUSHIKIDENKAIETSUCHINGUHOHO
JPS63186899A (en) * 1987-01-28 1988-08-02 Asahi Glass Co Ltd Method for dissolving tin oxide
JPH07207500A (en) * 1994-01-18 1995-08-08 Nishiyama Stainless Chem Kk Method for regenerating glass plate and device therefor
JP2003268600A (en) * 2002-03-14 2003-09-25 Nishiyama Stainless Chem Kk Electrolytic peeling method by high-velocity polarity inversion
JP2004137545A (en) * 2002-10-17 2004-05-13 Nippon Steel Corp Electrode for continuous treatment of metallic strip

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5175638A (en) * 1974-12-26 1976-06-30 Stanley Electric Co Ltd MUSETSUZOKUSHIKIDENKAIETSUCHINGUHOHO
JPS63186899A (en) * 1987-01-28 1988-08-02 Asahi Glass Co Ltd Method for dissolving tin oxide
JPH07207500A (en) * 1994-01-18 1995-08-08 Nishiyama Stainless Chem Kk Method for regenerating glass plate and device therefor
JP2003268600A (en) * 2002-03-14 2003-09-25 Nishiyama Stainless Chem Kk Electrolytic peeling method by high-velocity polarity inversion
JP2004137545A (en) * 2002-10-17 2004-05-13 Nippon Steel Corp Electrode for continuous treatment of metallic strip

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