TWI274616B - Method and system for removing thin metal film - Google Patents

Method and system for removing thin metal film Download PDF

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Publication number
TWI274616B
TWI274616B TW092127919A TW92127919A TWI274616B TW I274616 B TWI274616 B TW I274616B TW 092127919 A TW092127919 A TW 092127919A TW 92127919 A TW92127919 A TW 92127919A TW I274616 B TWI274616 B TW I274616B
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Taiwan
Prior art keywords
electrode
metal
electrolyte
thin film
metal plate
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TW092127919A
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Chinese (zh)
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TW200405838A (en
Inventor
Hiroyuki Daiku
Hidehiko Maehata
Masanori Tsukahara
Shogo Hamada
Tetsuya Inoue
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Hitachi Shipbuilding Eng Co
Hitz Hi Technology Corp
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Publication of TW200405838A publication Critical patent/TW200405838A/en
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F5/00Electrolytic stripping of metallic layers or coatings
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C23/00Other surface treatment of glass not in the form of fibres or filaments
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F3/00Electrolytic etching or polishing
    • C25F3/02Etching
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F7/00Constructional parts, or assemblies thereof, of cells for electrolytic removal of material from objects; Servicing or operating

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Electrochemistry (AREA)
  • Metallurgy (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Electrolytic Production Of Metals (AREA)

Abstract

A system for removing a thin metal film comprising an inclining metal plate electrode (21) for guiding a downward electrolyte flow, an auxiliary electrode (22) placed on the upstream or downstream side of the metal plate electrode (21) such that a part of the auxiliary electrode is immersed into the electrolyte, and a power supply (23) for applying a DC voltage to the both electrodes. The system is used to remove a metal thin film (24a) on the surface of an insulator (24) by making the electrolyte (26) flowing down the metal plate electrode (21) strike against the metal thin film (24a) under a state where the DC voltage is applied to the metal plate electrode (21) and the auxiliary electrode (22).

Description

1274616 玖、發明說明: [發明所屬之技術領域] +本發明係關於一種例如由蒸鍍或電鍍所形成之金屬薄 膜在不滿足品質管理基準的情況下,自基板將該金屬薄膜 加以除去之方法以及用以實施該方法之裝置。 [先前技術] 在光學性能(穿透率等)、機械性能(平坦度等)優異之高 功旎玻璃基板係用於例如平面面板顯示器。但是,由於價 格昂貴,當其表面所形成之金屬薄膜不滿足品質管理基準 的“況下,乃希望將該金屬薄膜除去而再利用。 此金屬薄膜之除去方法有藉由化學蝕刻來除去之方法 。此方法係如第18圖所示般,將表面形成有欲除去之金 屬薄膜的基板2浸潰於可將金屬薄膜以化學反應來溶解之 化學液1中,藉此除去金屬薄膜(可參見例如曰本特開平 6-321581號公報、曰本特開平9_86968號公報)。 但是,以化學敍刻來除去之方&,由於使用強酸或強 驗之化學液,所以有以下問題·· 1) 由於使用上必須特別注意,作業性乃變差。 2) 必須對裝置賦予耐蝕性,成分會增加。 3) 化學液基本上係用完即丟棄,會產生大量廢液。 4) 使用後,化學液之廢液處理困難。 本發明係鑒於上述以往之問題所做的改良,其目的在 於提供一種無須使用強酸或強鹼之化學液且無須進行精密 之位置控制即可以原則上非接觸方式將金屬薄膜高效率除 Ϊ274616 去之方法以及用以實施此方法之裝置。 [發明内容] 本發明之第i金屬薄膜之除去方法,係使用由金屬平 板電極(呈傾斜狀配置,用以引導電解液之流下)、辅助電 極(位於金屬平板電極21之上游側或下游側,以—部分合 浸潰於電解液中所配置者)以及直流電壓電源(對前述兩; 極施加電壓)所構成之本發明之第^屬薄膜之除去裝置, ,金屬平板電極與輔助電極被施加直流電㈣狀態下,使 得自該金屬平板電極上流下之電解液與絕緣物表面之金屬 薄膜衝撞,來將金屬薄膜除去。 依據第1本發明’無須使用強酸或強驗之化學液且無 須進行喷嘴電極龍緣物表面之金屬薄膜之精密位置控制、 ’即能以非接觸方式將金屬薄臈高效率除去而不會損及絕 又,本發明之第2金屬薄膜之除去方法,係使用本發 明之弟2金屬薄膜之除去裝置(為前述本發明之第!金屬薄 膜之除去裝置中,以橫跨金屬平板電極與輔助電極間的方 式在此兩電極之下方配置底面電極,此底面電極亦被直流 電歷電源施加與輔助電極呈同極之直流電壓),在前述本發 明之第1金屬薄膜之除去方法中,在絕緣物之背面侧所配 置之底面電極亦被施加直流電壓的狀態下,使得自該金屬 平板電極上流下之電解液與絕緣物表面之金屬薄膜衝撞, 來將金屬薄膜除去。 藉此,可更加助長第丨本發明之作用效果。 Ϊ274616 卜:别述第1或苐2本發明中,若設置一移動機構,使 貝於電解液中之絕緣物以及金屬平板電極中之至少一 移動目Γ於另—者做移動’在絕緣物與金屬平板電極做相對 移動的同時來去除金屬薄膜,則可除去廣範圍的金屬薄膜 本發明之第3金屬薄膜之除去方法,係於前述第 “明中,使用在金屬平板電極之絕緣物進入側 奘罢+ 丁心不A 3之苐3金屬薄膜之除去 、* "抑制早期之電解液對絕緣物端部側之入侵。 藉此,可防止麻點狀之金屬薄膜的發生。 又’本發明之第4金屬薄膜之除去方法,係於前述第 弟、3本發明中,使用將金屬平板電極做成旋轉自如的電 ’並在此電極之金屬薄膜接觸部設置研磨基材、或是具 :對電極之金屬薄膜接觸部供給研磨基材之供給機構之 =明之第4金屬薄膜之除去裝置,以位於此電極之金屬 潯膜接觸部之研磨基材來擦過金屬薄膜之表面。 此第4本發明,可將電解熔解析出所殘留之 去除。 [實施方式] 為了更詳細地說明本發明’乃參照所附圖式做說明。 —首先’本發明之第i金屬薄膜之除去裝置之一例係示 於第1圖〜第3圖。 於第i圖〜第3圖中,21係與後述之絕緣物24具有大 致相同寬度、在電解液26之上方以傾斜狀直立設置之金 I274616 板電極22係一下端部浸潰於雷紘 > ^ ^ ^ r- 1 /又/貝於電解液20之輔助電極 23係直流電壓電源,24 #读 例如舍越由 …又,貝於加工槽25内之電解液( 薄膜24 絕緣物,其表面形成有待除去之金屬 …。又’ Μ係表示電解熔解析出部,v係表示閥。 ,弟1圖所示之例係藉由系28將電解液槽27内之電解 液26送往金屬平板電極 稍助冤極22係一圓柱狀之物 絕緣物24之表面之全屬壤胺 設置。 之金屬相24a呈非接觸狀態做直立 又,第2圖與第3圖所示之例,輔助電極22係形成為 列如可旋轉自如之輥狀而與金屬平板電極2ι做平行配置 ’使得此輔助電極22與絕緣物24表面之金屬薄膜“a接 觸又,如第3圖所示般,加工後之電解液26係回收於 電解液槽27,所回收之電解液以過濾器3〇過據後送往金 屬平板電極21,藉此,電解液26可循環使用。又,輥狀 之辅助電極22亦能以與絕緣物24表面之金屬薄膜2乜呈 非接觸狀態來固定配置。 上述第1本發明係基於以下原理來除去金屬薄膜2乜 ① 使電解液2 6自金屬平板電極2 1朝金屬薄膜2 4 a流 動,形成電性連續流26a。 ② 若以金屬平板電極21,則會形成由直流電壓電源2 3 一金屬平板電極21 —連續流26a—金屬薄膜24a—電解液 26—輔助電極22—直流電壓電源23所構成之封閉電路。 ③ 一旦形成前述電路,則電壓與電流會成為第4圖所 1274616 示之曲線。一旦超# 極21以及金屬薄膜 圖中…壓,則金屬平板電 細氣泡。又,一曰、^之表面開始產生氫、氧離子以及微 伴隨於此氡泡:=B電壓,則電流開始急速地上升, 座生1也會急速地增加。 ④進而,一旦.、 比M^ σ過C電壓,則電壓與電流大致成為正 比關係,下述①戎 薄膜之溶解析出 仏疋律大致成立,可見到金屬 此時,絕緣物24,妙不4^24a之除去加工乃得以進行。 尨人M 田Γ、Λ不會發生電解熔解析出。又,D電壓 ....^ . 最小電壓值,亦即分解電壓,由電極材 枓(表面活性度)、蕾 電解液》辰度、線路電阻等所決定。 ① W=7? 1 · "· k·卜 t · · β 1 ·、熔解析出效率(%) π 2 :電流效率(%) k :電化學當量(mg/c) I :電解電流(A) t :電解時間(sec) 盗上述第1本發明(第2、3圖所示之例除外)由於為非接 f之加工法’所以不會對絕緣物造成損傷。再者,電極與 金屬薄膜間無須高精度之位置控制。x,非化學除去而是 利用電解炼解析出之加工,只要為可流通電流之電解液即 可’乃可使用NaN〇3、NaC1等之中性鹽電解液,所以作業 性優異、電解液之廢液處理亦可輕易進行。又,第2 3圖 所示之帛1本發明之接觸也僅是輥狀之辅助電極Μ,基本 上與前述相同。 土 1274616 另方面,前述裳1 4* 動來咚土 ^ 乐1本發明中,例如隨著絕緣物24移 所2 薄膜24a而成為最終端的情況,如第5圖⑷ 婉全屬賴24a與輔助電極22間之距離會變大,流 c%之電流量相較於電解 寬机政率會變差, 不 合#弟5圖(b)所示般,最終金屬薄膜24a 於下游側(第5圖中之紙面左側)。 缘物7,於帛1本發明中,只要如第6圖所示般,在絕 琢初24之下游相,丨以 24之尸 圖之紙面左側)端部設置與絕緣物 24之^ λ致相同厚度之導電體板3 1,則即使絕緣物 23—属冬端通過輔助電# 22 ’藉由形成由直流電壓電源 體板31—平板電極21—連續流仏-金屬薄膜24a-導電 成之刼^解液26—輔助電極22-直流電壓電源23所構 留閉電路,可防止電流效率之降低,金屬薄膜 體= 下游側端部。又,為了形成上述封閉電路,導電 輔助^ ¥極移動方向之長度必須較金屬平板電極21與 輔助電極22間之間隔a為長。 n血P使疋取代第6圖所不之在絕緣物24之下游側端 =置:絕_ 24呈大致相同厚度之導電體板31,改為 Μ· T般將電性料析出所使用之電極以陰極(例 板電極21)'陽極(例如輔助電極22戌互複數配 置:物’或是如第7圖⑻所示般以圓冑32之内側為陰極 、外側為陽極者複數個配置之物,亦可達成與設置導電體 扳3 1同樣的作用效果。 又,第7目⑷所示者係陰極與陽極以絕緣體33做連 12 1274616 結之物。 其次,本發明之第2金屬薄膜 第8圖。於第8圖中 、矛、^置之一例示於 29係板跨金屬平板電極21斑 電極22間之在該等電極21力下方 21與辅助 構成係與第3圖所示之例相同。 &面電極,其他 另一方面,在該等第!、第 析二二部1274616 发明, invention description: [Technical field to which the invention pertains] + The present invention relates to a method for removing a metal thin film from a substrate without satisfying a quality management standard, for example, a metal thin film formed by vapor deposition or electroplating And means for carrying out the method. [Prior Art] A high-performance glass substrate excellent in optical properties (penetration ratio, etc.) and mechanical properties (flatness, etc.) is used for, for example, a flat panel display. However, since it is expensive, when the metal film formed on the surface does not satisfy the quality management standard, it is desirable to remove the metal film and reuse it. The method of removing the metal film has a method of removing by chemical etching. The method is as shown in FIG. 18, and the substrate 2 on which the metal thin film to be removed is formed is immersed in the chemical liquid 1 which can dissolve the metal thin film by a chemical reaction, thereby removing the metal thin film (see also For example, JP-A-H06-321581, JP-A-H09-86968). However, the chemical removal of the square & ) Due to the special care required, the workability is deteriorated. 2) Corrosion resistance must be imparted to the device, and the composition will increase. 3) The chemical liquid is basically discarded when it is used up, and a large amount of waste liquid is generated. 4) After use, The treatment of the waste liquid of the chemical liquid is difficult. The present invention has been made in view of the above conventional problems, and an object thereof is to provide a chemical liquid which does not require the use of a strong acid or a strong alkali and which does not require precision. The position control is a method for removing the high efficiency of the metal film from the 274616 in a non-contact manner and a device for carrying out the method. [Explanation] The method for removing the ith metal film of the present invention is to use a metal plate electrode (in a slanted configuration for guiding the flow of the electrolyte), an auxiliary electrode (on the upstream side or the downstream side of the metal plate electrode 21, to be partially immersed in the electrolyte), and a DC voltage source (pair) The apparatus for removing a film of the invention according to the present invention, wherein the metal plate electrode and the auxiliary electrode are applied with a direct current (four) state, so that the electrolyte and the surface of the insulator flow from the metal plate electrode The metal film collides to remove the metal film. According to the first invention, it is not necessary to use a strong acid or a strong chemical liquid, and it is not necessary to perform precise position control of the metal film on the surface of the nozzle electrode edge, 'that can be in a non-contact manner The method for removing the second metal thin film of the present invention is to remove the metal thin crucible with high efficiency without damaging it. The apparatus for removing a metal thin film of the invention 2 (in the apparatus for removing a metal thin film according to the present invention, a bottom electrode is disposed below the two electrodes so as to straddle between the metal plate electrode and the auxiliary electrode, and the bottom electrode is also In the method of removing the first metal thin film of the present invention, in the method of removing the first metal thin film of the present invention, a DC voltage is applied to the bottom electrode disposed on the back side of the insulating material. The electrolyte flowing down from the metal plate electrode collides with the metal film on the surface of the insulator to remove the metal film. Thereby, the effect of the present invention can be further enhanced. Ϊ 274616 卜: Others 1 or 2 In the present invention, if a moving mechanism is provided, at least one of the insulation in the electrolyte and the metal plate electrode is moved to the other side to move while the insulator and the metal plate electrode are relatively moved. The method of removing the metal thin film and removing the wide range of metal thin films of the present invention is as described in the above-mentioned "Ming, The insulating material plate with the metal electrodes into the heart does not stout stop 3 + D 3 of Ti removal of the metal thin film side A, * " inhibit early invasion of the electrolyte side of the end portion of the insulator. Thereby, the occurrence of a pitting-like metal film can be prevented. Further, in the method of removing the fourth metal thin film of the present invention, in the above-described third and third inventions, a metal plate electrode is rotatably electrically connected, and a polishing substrate is provided at a metal thin film contact portion of the electrode. Alternatively, the fourth metal film removing device for supplying the polishing substrate to the metal film contact portion of the electrode is wiped over the surface of the metal film by the polishing substrate located at the contact portion of the metal film of the electrode. According to the fourth aspect of the invention, the electrolytic melting can be analyzed and removed. [Embodiment] The present invention will be described in more detail with reference to the accompanying drawings. - First, an example of the apparatus for removing the i-th metal film of the present invention is shown in Figs. 1 to 3 . In the first to third figures, the 21st and the insulator 24 which will be described later have substantially the same width, and the gold I274616 plate electrode 22 which is erected above the electrolyte 26 in an inclined manner is immersed in the Thunder>; ^ ^ r r 1 / / / / in the electrolyte 20 of the auxiliary electrode 23 is a DC voltage power supply, 24 # read, for example, the reciprocal by ... again, the electrolyte in the processing tank 25 (film 24 insulation, its The surface is formed with a metal to be removed. . . . ' Μ indicates the electrolytic melting analysis portion, and v indicates the valve. The example shown in the middle of FIG. 1 sends the electrolyte 26 in the electrolytic solution tank 27 to the metal by the system 28 . The plate electrode slightly assists the bungee 22 to be a surface of the columnar insulator 24 which is entirely of the surface amine. The metal phase 24a is erect in a non-contact state, and the examples shown in Fig. 2 and Fig. 3 are auxiliary. The electrode 22 is formed in a column shape such as a rotatable roller and is disposed in parallel with the metal plate electrode 2' such that the auxiliary electrode 22 is in contact with the metal film "a" on the surface of the insulator 24, as shown in FIG. The electrolyte 26 is recovered in the electrolyte tank 27, and the recovered electrolyte is filtered. After passing through the metal plate electrode 21, the electrolyte 26 can be recycled. Further, the roller-shaped auxiliary electrode 22 can be fixed in a non-contact state with the metal film 2乜 on the surface of the insulator 24. The first invention described above removes the metal thin film 2乜1 based on the following principle to cause the electrolytic solution 26 to flow from the metal flat electrode 2 1 toward the metal thin film 2 4 a to form an electrically continuous flow 26a. 2 If the metal flat electrode 21 is used Then, a closed circuit composed of a DC voltage source 2 3 - a metal plate electrode 21 - a continuous flow 26a - a metal film 24a - an electrolyte 26 - an auxiliary electrode 22 - a DC voltage source 23 is formed. 3 Once the aforementioned circuit is formed, the voltage is formed. The current will become the curve shown in Fig. 4, paragraph 1474616. Once the super-electrode 21 and the metal film are pressed, the metal plate is electrically fine. In addition, the surface of the 曰, ^ begins to generate hydrogen, oxygen ions and micro-companion. In this bubble: = B voltage, the current starts to rise rapidly, and the seat 1 will increase rapidly. 4 Further, once the voltage exceeds the C voltage by M^ σ, the voltage and the current are approximately proportional. It is said that the law of dissolution and precipitation of the film is generally established, and it can be seen that the metal 24, the insulation 24, and the removal of the mold 4 can be carried out. The M人M field Γ, Λ does not undergo electrolytic melting analysis. Also, the D voltage....^. The minimum voltage value, that is, the decomposition voltage, is determined by the electrode material (surface activity), the bud electrolyte, the line resistance, etc. 1 W=7? 1 · &quot ;· k·卜 t · · β 1 ·, melting analysis efficiency (%) π 2 : current efficiency (%) k : electrochemical equivalent (mg/c) I : electrolysis current (A) t : electrolysis time (sec The first invention (except the examples shown in Figs. 2 and 3) is stolen because it is a processing method that is not connected to f, so that the insulation is not damaged. Furthermore, there is no need for high-precision position control between the electrode and the metal film. x, which is a chemically-resolved process that is not chemically removed, as long as it is an electrolyte that can flow current, and can use a neutral salt electrolyte such as NaN〇3 or NaC1, so that it has excellent workability and electrolyte solution. Waste liquid treatment can also be carried out easily. Further, the contact 1 of the present invention shown in Fig. 2 is only a roller-shaped auxiliary electrode, and is basically the same as described above. In addition, in the present invention, for example, the case where the insulator 24 is moved to the second film 24a becomes the most terminal, as shown in Fig. 5 (4), all of which belong to 24a and auxiliary. The distance between the electrodes 22 will become larger, and the current amount of the flow c% will be worse than that of the electrolysis wide machine. As shown in Fig. 5(b), the final metal film 24a is on the downstream side (Fig. 5). On the left side of the paper). In the present invention, as shown in Fig. 6, as shown in Fig. 6, in the downstream phase of the primary 24, the end of the paper on the left side of the corpse of 24 is provided with the insulator 24 The conductor plate 3 1 of the same thickness is electrically conductive even if the insulator 23, which is a winter end, is formed by the auxiliary power source 22' by the DC voltage power source body plate 31 - the plate electrode 21 - the continuous flow - the metal film 24a -刼^ Solution 26—Auxiliary electrode 22—The DC voltage source 23 is constructed to be a closed circuit that prevents current efficiency from decreasing. The metal film body = the downstream end. Further, in order to form the above-described closed circuit, the length of the direction in which the conductive auxiliary electrode is moved must be longer than the interval a between the metal plate electrode 21 and the auxiliary electrode 22. n blood P makes 疋 replace the downstream side end of the insulator 24 which is not shown in Fig. 6 = the conductor plate 31 which is substantially the same thickness as the _ 24, and is used to precipitate the electric material like Μ·T The electrodes are arranged in a plurality of cathodes (for example, the plate electrodes 21)' anodes (for example, the auxiliary electrodes 22 are arranged in plural numbers: or as shown in FIG. 7 (8), with the inside of the circle 32 as the cathode and the outside as the anode. The object can also achieve the same effect as the provision of the conductor plate 31. Further, in the seventh item (4), the cathode and the anode are connected by the insulator 33 as a 12 1274616. Next, the second metal film of the present invention. Fig. 8. In Fig. 8, one of the spears and one of the spears is illustrated between the 29-plate cross-metal plate electrode 21 and the spot electrode 22 under the force of the electrode 21 and the auxiliary structure and the third figure. The same example. & surface electrode, on the other hand, in the second!

5極與薄膜之距離會遠離,電流會逐漸消 解析出,所以當絕緣物24表 進仃熔 衣向覓廣的情況下,盔法脾矣 面所形成之金屬薄臈24a整體加以除去。 、 Γ中疋以’在弟1、第2本發明中,設置使得浸潰於電解 m金屬平板電極21中至少—者相對於 另一者做移動之移動機構,—邊令絕緣物24愈金板 電極做相對移動-邊除去金屬薄膜24 圍的金屬薄膜24a。此時,在第丨與第2本==The distance between the 5 pole and the film is far away, and the current is gradually resolved. Therefore, when the insulator 24 is placed in the smelting coat, the metal thin ridge 24a formed by the spleen surface is removed as a whole. In the first and second inventions, the middle body is provided with a moving mechanism that causes at least one of the electrolytic metal plate electrodes 21 to move relative to the other, and the insulator 24 is made of gold. The plate electrodes are relatively moved to remove the metal thin film 24a around the metal film 24. At this time, in the third and second ==

:屬平板電極21之寬度為w(cm)、以相對移動速度為 V(Cm/min)、以電流為1(A),則以具有 , 〇. 1 ^ I/(W X v) ^ 〇.〇3 關係之範圍的相對移動速度來移動為佳。 使得此金屬平板電極21相對於另一者移動之際,在第 1與第2本發明中,例如使得被施加正電壓之輔助電極22 位於被施加負電壓之金屬平板電和5 21之上游側、亦即以 辅助電極22較金屬平板電極21先通過絕緣物24表面之 金屬薄膜24a的方式來配置為佳。 13 1274616 其理由在於,電解熔解析出係被施加正電壓之陽極部 分出現熔解析出,所以金屬薄膜24a之熔解析出係自接: 被施加負電壓之處、例如在第1圖〜第3圖、第5圖以及 第6圖、第8圖所示之例子中自位於金屬平板電極η下 方之金屬薄臈24a處炫解析出之故。亦即,若往反方向移 動,則金屬薄膜24a之炼解析出部分會通過電極間,乃益 法形成前面所提到之封閉電路,而無法進行連續性溶解二 出。又,為了防止陽極之溶解析出,對陽極電極施以 麵之鍍敷乃為所希望者。 於前述第卜第2本發明中’當金屬平板電極 於絕緣物24移動之際,若輔助電極22被固定,則電極乂 距離會隨著金屬平板電極21的移動而改變,電法 會發生變化,無法進行金屬薄膜24a之均-的除去。机 在廷種情況下,將輔助電極22如 般與金屬平板電極21平行配置,…苐3圖所示 解決此問題。 〜丁配置’使-兩者同時移動即可 “又二在第^第2本發明中,若金屬薄膜24a之除去The width of the plate electrode 21 is w (cm), the relative movement speed is V (Cm / min), and the current is 1 (A), and has ,. 1 ^ I / (WX v) ^ 〇. It is better to move the relative movement speed of the range of 〇3 relationship. When the metal plate electrode 21 is moved relative to the other, in the first and second inventions, for example, the auxiliary electrode 22 to which a positive voltage is applied is located on the upstream side of the metal plate to which the negative voltage is applied and the 521. That is, it is preferable that the auxiliary electrode 22 is disposed so as to pass through the metal thin film 24a on the surface of the insulator 24 before the metal flat electrode 21. 13 1274616 The reason is that in the electrolytic melting analysis, the anode portion to which a positive voltage is applied is melted and analyzed, so that the melting of the metal thin film 24a is self-contacting: where a negative voltage is applied, for example, in FIGS. 1 to 3 In the example shown in Fig. 5, and Fig. 6 and Fig. 8, the metal thin crucible 24a located below the metal plate electrode η is decimated. That is, if it moves in the opposite direction, the refining portion of the metal thin film 24a passes through the electrodes, and it is advantageous to form the closed circuit mentioned above, and it is impossible to perform continuous dissolution. Further, in order to prevent the anode from being dissolved and precipitated, it is desirable to apply the surface to the anode electrode. In the foregoing second invention, when the metal plate electrode moves on the insulator 24, if the auxiliary electrode 22 is fixed, the electrode 乂 distance changes with the movement of the metal plate electrode 21, and the electric method changes. The uniform removal of the metal thin film 24a cannot be performed. In the case of the machine, the auxiliary electrode 22 is arranged in parallel with the metal plate electrode 21 as shown in Fig. 3 to solve this problem. 〜丁Configuration' enables both to move at the same time. "In the second invention, if the metal film 24a is removed

Si進I::解液%漏“被覆於絕緣物24上,則絕緣 而〇P在通過金屬平板電極21或輔助電極22 1 生電解炫解析出。此乃由於雖通常電極 二 電…強度)最強,熔解析出僅在電極間發生,惟、Λ ( 電極間同等電場強度之:會產生電場集中而成為與 再者,在絕緣物24之端部的電場不均一,金屬薄媒 1274616 24a之除去也會不均一,於是金屬薄膜24a在絕緣物24之 端部會如第9圖所示般以麻點狀殘留。又,第9圖中之 24b係顯示呈麻點狀殘留之金屬薄膜。 即使此種殘留麻點狀金屬薄膜24b之部分通過金屬平 板電極2 1,金屬薄膜也會因麻點狀部分無法做連續性熔解 析出,而無法形成前面所提到之封閉電路,金屬薄膜2朴 將無法除去而殘留。 是以,在第1或第2本發明中,在金屬平板電極21之 絕緣物24進入侧設置抑制電解液26入侵構件,例如使得 =有與絕緣物24寬度大致相同寬度的第1〇圖所示之橡膠 製壁34a以儘量接近絕緣物24表面的方式來設置,或是將 1有與絕緣物24寬度大致相同寬度的第u圖所示之橡膠 製輥34b以彈簧35壓貼於絕緣物24之表面來設置,則可 抑制電解液26早期入侵於絕緣物24之端部側,可防止麻 點狀金屬薄膜24b之發生。此乃第3本發明。 又,在則述第1〜第3本發明中,由於電流經由電解液 %流動’所以在電解液26中流動之電流會造成金屬薄膜 24a之熔解析出的惡化。 疋以,在第1〜第 則之金屬平板電極21與輔助電極22之間如第12圖月 般以儘量接近絕耗24表面的方式設置諸如具有與释 物24之寬度大致相同寬度之絕緣物壁刊,即可減少洛 電解液26之電流,可提升金屬薄膜24a之熔解析出效^ 又’在前述第1〜第3本發明中,雖有在避免損傷舜 15 1274616 物24的前提下高效率地除去金屬薄膜24a的情況,惟亦有 由於在電解液26中流動之電流將金屬薄膜2乜熔解析出而 除去金屬薄膜24a,結果在電解熔解析出殘留殘量之膜的 情況。 是以,在第1〜第3本發明中,可取代金屬平板電極 21,採用旋轉自如之電極37,且在此電極37之與金脣薄 膜24a接觸部設置研磨基材,或是具備可對電極37'與金屬Si into I:: % solution leaching "overlying the insulator 24, the insulation is 〇P is resolved by electrolysis of the metal plate electrode 21 or the auxiliary electrode 22 1 . This is because the electrode usually has two electrodes... strength) The strongest, the melt analysis occurs only between the electrodes, but Λ (the same electric field strength between the electrodes: the electric field is concentrated and becomes the same, the electric field at the end of the insulator 24 is not uniform, the metal thin material 1274616 24a The removal of the metal thin film 24a at the end of the insulator 24 may be in the form of pitting as shown in Fig. 9. Further, 24b in Fig. 9 shows a metal thin film remaining in a punctiform shape. Even if part of the residual punctiform metal film 24b passes through the metal plate electrode 2 1, the metal film cannot be continuously melted out due to the punctiform portion, and the closed circuit mentioned above cannot be formed, and the metal film 2 is not formed. In the first or second invention, the intrusion member for suppressing the electrolyte solution 26 is provided on the inlet side of the insulator 24 of the metal plate electrode 21, for example, so that the width of the insulator 24 is substantially the same as that of the insulator 24. 1st of width The rubber wall 34a is shown as being as close as possible to the surface of the insulator 24, or the rubber roller 34b shown in Fig. 1 having a width substantially the same as the width of the insulator 24 is pressed against the insulator by the spring 35. When the surface of the object 24 is provided, the electrolyte solution 26 can be prevented from invading the end portion of the insulator 24 at an early stage, and the occurrence of the punctiform metal film 24b can be prevented. This is the third invention. In the third aspect of the invention, since the current flows through the electrolyte solution %, the current flowing in the electrolyte solution 26 causes the deterioration of the melting of the metal thin film 24a. In the first to the third metal plate electrodes 21 and The auxiliary electrode 22 is disposed between the auxiliary electrodes 22 as close as possible to the surface of the insult 24, such as an insulator wall having a width substantially the same as the width of the discharge member 24, thereby reducing the current of the electrolyte 26 and improving the current. In the first to third inventions, the metal film 24a is efficiently removed while avoiding damage to the material 24, but it is also due to the fact that the metal film 24a is efficiently removed. Current flowing in the electrolyte 26 When the metal thin film 2 is melted and analyzed, and the metal thin film 24a is removed, the residual residual amount of the film is analyzed by electrolytic melting. Therefore, in the first to third inventions, the metal flat plate electrode 21 can be used instead of the rotation. The electrode 37 is provided with a polishing substrate at the contact portion of the electrode 37 with the gold lip film 24a, or a counter electrode 37' and a metal

薄膜24a之接觸部供給研磨基材之供給機構。依據此種構 成,能以位於電極37與金屬薄膜24a之接觸部的研磨基材 擦過金屬薄膜24a表面,將電解熔解析出中所殘留之膜完 全除去。此為第4本發明。 J珂V固邵配置The contact portion of the film 24a is supplied to a supply mechanism of the polishing substrate. According to this configuration, the surface of the metal thin film 24a can be wiped by the polishing substrate located at the contact portion between the electrode 37 and the metal thin film 24a, and the film remaining in the electrolytic fusion analysis can be completely removed. This is the fourth invention. J珂V solid-shoring configuration

可通水之研磨基材的旋轉自如的棒狀電極37中心部, 電解液槽27供給電解液26,使得電解液%自棒狀電 37之外圍部流出之例子。又’帛14圖所示之例子中, 將第13圖所示之辅助電極22與棒狀電極37做平行配 ’第15圖所示之例子中,係將帛13圖所示之棒狀^丁^ 改為下面配置有可通水之研磨基材之旋轉自如的碟狀電 37。又’第16圖所示之例子係將第14圖所示之輔助電 22形成輥狀而與絕緣物24表面之金屬薄膜2乜接觸, 17圖所示之例子,係取代對電極37之内部供給電解液 改為自外部供給電解液26。 在以上之例子中係顯示了在 的接觸部配置研磨基材之情況, 電極37之與金屬薄臈24a 但亦可於電極27不配置 16 1274616 研磨基材’而對電極37之與金屬薄膜24a的接觸部供給研 磨基材。 以下’針對用以確認本發明效果所進行之實施結果做 說明。 A·第1本發明之實施例(之一) 使用第3圖所示構成之本發明之第1金屬薄膜之除去 裝置(金屬平板電極之寬度:1〇〇〇inm),以下述的加工條件 來實施本發明之第1金屬薄膜之除去方法,結果可將在 馨 lOOOmmX l〇〇〇mm之玻璃基板上所蒸鍍之1〇〇〇>< 1〇.1()爪厚 度之銘薄膜有效地除去,可進行玻璃基板之再生。又,除 了將報狀之輔助電極以相對於玻璃基板呈非接觸的方式來 固定配置,將電流變更為30〇A以外,以相同之加工條件 來實施本發明之第2金屬薄膜之除去方法,結果與前述同 樣,可將在玻璃基板上所蒸鍍之鋁薄膜有效地除去,可進 行玻璃基板之再生。 [加工條件] 電解液:20%NaCl #An example in which the electrolyte solution 26 is supplied to the center portion of the rod-shaped electrode 37 which is rotatable by the water-permeable polishing substrate, and the electrolyte solution 26 is allowed to flow out from the peripheral portion of the rod-shaped electricity 37. In the example shown in Fig. 14, the auxiliary electrode 22 shown in Fig. 13 is arranged in parallel with the rod electrode 37. In the example shown in Fig. 15, the rod shape shown in Fig. 13 is shown. Ding ^ is changed to a disk-shaped electric 37 which is rotatably arranged to have a water-permeable abrasive substrate. Further, in the example shown in Fig. 16, the auxiliary electric power 22 shown in Fig. 14 is formed into a roll shape and is in contact with the metal thin film 2 of the surface of the insulator 24, and the example shown in Fig. 17 is substituted for the inside of the counter electrode 37. The supply of the electrolyte is changed from the external supply of the electrolyte 26. In the above example, the case where the polishing substrate is disposed at the contact portion is shown, the electrode 37 is thin with the metal thin layer 24a, but the electrode 27 may not be disposed with the electrode 12 and the metal film 24a. The contact portion supplies the abrasive substrate. The following description will be made on the results of the implementation performed to confirm the effects of the present invention. A. The first embodiment of the present invention (1) The first metal film removing device (the width of the metal plate electrode: 1 〇〇〇inm) of the present invention having the configuration shown in Fig. 3 is used, and the following processing conditions are used. The method for removing the first metal thin film of the present invention is carried out, and as a result, a thickness of 1 〇〇〇><1〇.1() of the thickness of the claw can be deposited on a glass substrate of 100 nm×10 mm. The film is effectively removed, and the glass substrate can be regenerated. Moreover, the second metal thin film removal method of the present invention is carried out under the same processing conditions except that the auxiliary electrode of the report is fixedly disposed so as not to be in contact with the glass substrate, and the current is changed to 30 〇A. As a result, in the same manner as described above, the aluminum thin film vapor-deposited on the glass substrate can be effectively removed, and the glass substrate can be regenerated. [Processing conditions] Electrolyte: 20% NaCl #

噴出流量:約30L/min 施加電壓:約100V 電流:150A 玻璃基板移動速度:1 m/min B ·第1本發明之實施例(之二) 使用第3圖所示構成之本發明之第1金屬薄膜之除去 裝置’如第6圖所示般,在i〇〇〇mmX 1〇〇〇nim之玻璃基板 17 !274616 (厚度0.7mm)之終端設置有相同厚度之碳板的狀態下,以 下述加工條件,實施本發明之第丨金屬薄膜之除去方法, 結果可將在玻璃基板上所蒸鍍之厚度1〇〇〇xl〇_1Gm之鋁薄 膜有效地除去直到端部,可進行玻璃基板之再生。 [加工條件]Discharge flow rate: about 30 L/min Applied voltage: about 100 V Current: 150 A Glass substrate moving speed: 1 m/min B · First embodiment of the present invention (Part 2) The first aspect of the present invention having the configuration shown in Fig. 3 As shown in Fig. 6, in the state in which the carbon plate of the same thickness is provided at the end of the glass substrate 17 !274616 (thickness: 0.7 mm) of i〇〇〇mmX 1〇〇〇nim, the following is the following: The processing conditions are described, and the method for removing the second metal thin film of the present invention is carried out. As a result, the aluminum thin film having a thickness of 1 〇〇〇 x 1 〇 1 Gm vapor-deposited on the glass substrate can be effectively removed until the end portion, and the glass substrate can be processed. Regeneration. [Processing conditions]

電解液:5%NaCl 噴出流量:約30L/min 施加電壓:約1 〇〇V 電流:300A 玻璃基板移動速度:lm/min C·第3本發明之實施例(之一) 使用第10圖所示構成之本發明之第3金屬薄膜之除去 裝置’以下述加工條件,實施本發明之第3金屬薄膜之除 去方法’結果可將在l〇〇〇mm><1〇〇〇mm之玻璃基板(厚度 0.7mm)上所蒸鑛之厚度ioooxio-wm之鋁薄膜有效地除去 直到端部,可進行玻璃基板之再生。 [加工條件]Electrolyte: 5% NaCl Jet flow rate: about 30 L/min Applied voltage: about 1 〇〇V Current: 300 A Glass substrate moving speed: lm/min C. Third embodiment of the present invention (one) Using Figure 10 The third metal thin film removing device of the present invention is configured to perform the method for removing the third metal thin film of the present invention under the following processing conditions. As a result, the glass of 10 mm><1 mm can be obtained. The aluminum film of the thickness ioooxio-wm of the vaporized ore on the substrate (thickness 0.7 mm) is effectively removed until the end portion, and the glass substrate can be regenerated. [Processing conditions]

電解液:5%NaCl 喷出流量:約30L/min 施加電壓:約1 〇 〇 V 電流:300A 玻璃基板移動速度:lm/min 抑制入侵構件:橡膠製壁 D.第3本發明之實施例(之二) 18 1274616 #吏用第12圖所示構成之本發明之第3金屬薄膜之除去 裝置’以下述加工條件,實施本發明之第3金屬薄膜之除 去方法,結果即使相較於其他實施例提高ι〇%移動速度, 仍可將在U)00mmX1_mm之玻璃基板(厚度〇7画)上所 蒸錢之厚度l_XlG.H)m之纟呂薄膜有效地除去,可進行玻 璃基板之再生。 [加工條件] 電解液·· 5%NaCl 贺出流量:約30L/minElectrolyte: 5% NaCl Discharge flow rate: about 30 L/min Applied voltage: about 1 〇〇V Current: 300 A Glass substrate moving speed: lm/min Inhibition of intrusion member: Rubber wall D. Third embodiment of the invention ( The second method of removing the third metal thin film of the present invention is carried out under the following processing conditions, and the result is as compared with other implementations. In the case of increasing the moving speed of ι〇%, the film of the thickness of l_XlG.H)m which is evaporated on the glass substrate of U)00mmX1_mm (thickness 〇7) can be effectively removed, and the glass substrate can be regenerated. [Processing conditions] Electrolyte·· 5% NaCl Concentration flow rate: about 30L/min

施加電壓:約1〇〇VApplied voltage: about 1 〇〇V

電流:300A 玻璃基板移動速度:l.lm/min 絕緣物壁:氯乙烯製壁 E.第4本發明之實施例 使用第16圖所示構成之本發明之第4金屬薄膜之除去 裝置,以下述加工條件,實施本發明之第4金屬薄膜之除 去方法’結果可將在1000mm X 1000mm之玻璃基板上所蒸 · 鍍之厚度l〇〇〇Xl〇’m之鋁薄膜完全除去而無殘留,可進 行玻璃基板之再生。 [加工條件] 電解液:20%NaCl 供給流量··約30L/min 棒狀電極旋轉數:600rpm 研磨劑磨粒·· #3000氧化鋁磨粒(混合於電解液中供給) 19 1274616Current: 300A Glass substrate moving speed: l.lm/min Insulator wall: Vinyl chloride wall E. Fourth embodiment of the present invention The fourth metal film removing device of the present invention having the configuration shown in Fig. 16 is used. The processing conditions and the method for removing the fourth metal thin film of the present invention are carried out. As a result, the aluminum film having a thickness of 10 〇〇〇 X 10 〇 'm which is evaporated and plated on a glass substrate of 1000 mm × 1000 mm can be completely removed without residue. The regeneration of the glass substrate can be performed. [Processing conditions] Electrolyte: 20% NaCl Supply flow rate · About 30 L/min Rod electrode rotation number: 600 rpm Abrasive abrasive particles · #3000 Alumina abrasive grains (mixed in electrolyte solution) 19 1274616

施加電壓:約100V 電流:300A 玻璃基板移動速度:1 m/min 上述實施例雖未與所有的申請專利範圍對應,惟不言 而喻的’即使是未在實施例中舉出之申請專利範圍的發明 ,亦可將絕緣物上所形成之金屬薄膜有效地除去,可進行 絕緣物之再生。Applied voltage: about 100 V Current: 300 A Glass substrate moving speed: 1 m/min Although the above embodiment does not correspond to all the patent claims, it is self-evident that even the patent application range not mentioned in the examples According to the invention, the metal thin film formed on the insulator can be effectively removed, and the insulation can be regenerated.

產業上可利用神 如上所述,本發明無須使用強酸或強鹼之化學液且無 須進行電極對絕緣物表面之金屬薄膜之精密位置控制,即 能以原則上非接觸方式將金屬薄膜高效率除去而不會損及 絕緣物,可達成半導體領域所使用之昂貴之功能性玻璃基 板之再生利用。 【圖式簡單說明】 (一)圖式部分Industrial Applicable God As described above, the present invention does not require the use of a chemical solution of a strong acid or a strong alkali and does not require precise position control of the metal film on the surface of the insulator by the electrode, that is, the metal film can be efficiently removed in a non-contact manner in principle. The use of expensive functional glass substrates used in the semiconductor field can be achieved without damaging the insulator. [Simple description of the schema] (1) Schema section

第1圖係顯示用以實施第1本發明之金屬薄膜之除去 裝置之一例之示意構成圖。 ” 第2圖係顯示用以實施第丨本發明之金屬薄膜之除去 裝置之第2例之示意構成圖。 于 第3圖係第2圖之整體構成圖。 第4圖係顯示以直流電壓電源__金屬平板電極—連續 流〜金屬薄膜一加工槽内之電解液〜辅助電極—直流電壓 電源形成封閉電路時之電壓與電流之關係圖。 ^ i 第5圖⑷係第1本發明中在終端部殘留金屬薄膜之原 20 1274616 因之說明圖,第 之圖。 5圖(b)係在、終端部殘留金屬薄膜之絕緣物 —第6圖係用以說明第丨本發明中避免在終端部發生金 屬薄膜殘留之方法之圖。 第7圖⑷(b)係用以說明第!本發明中避免在終端部發 生金屬薄膜殘留之另一態樣之圖。 ^第8 ®絲示用以實施第2本發明之金屬薄膜之除去 裝置之一例之示意構成圖。 第9圖係用卩說明在絕緣物之端部以麻點狀殘留之金 _ 屬薄膜之圖。 第10圖係顯示用以實施第3本發明之金屬薄膜之除去 裝置之一例之示意構成圖。 第11圖係顯示用以實施第3本發明之金屬薄膜之除去 裝置之其他例之示意構成圖。 第12圖係顯示用以實施第3本發明之其他實施例之金 屬薄膜之除去裝置之一例之示意構成圖。 第13圖係顯示用以實施第4本發明之金屬薄膜之除去 _ 裝置之一例之示意構成圖。 第14圖係顯示用以實施第4本發明之金屬薄膜之除去 裝置之第2例之示意構成圖。 第15圖係顯示用以實施第4本發明之金屬薄膜之除去 裝置之第3例之示意構成圖。 第16圖係顯示用以實施第4本發明之金屬薄膜之除去 裝置之第4例之示意構成圖。 21 1274616 第1 7圖係顯示用以實施第4本發明之金屬薄膜之除去 裝置之第5例之示意構成圖。 第1 8圖係以化學蝕刻來除去金屬薄膜之方法的說明圖 (二) 元件代表符號 1 化學液 2 基板 21 金屬平板電極 22 輔助電極 23 直流電壓電源 24 絕緣物 24a,24b 金屬薄膜 25 加工槽 26 電解液 26a 連續流 27 電解液槽 28 泵 30 過濾器 31 導電體板 32 圓筒 33 絕緣體 34a 橡膠製壁 34b 橡膠製輥 35 彈簧Fig. 1 is a schematic configuration view showing an example of a device for removing a metal thin film according to the first aspect of the invention. Fig. 2 is a schematic view showing a second example of a second embodiment of the apparatus for removing a metal thin film according to the present invention. Fig. 4 is a view showing the entire configuration of Fig. 2; __Metal plate electrode - continuous flow ~ metal film - electrolyte in the processing tank ~ auxiliary electrode - voltage and current when the DC voltage source forms a closed circuit. ^ i Figure 5 (4) is the first invention in The original part of the residual metal film in the terminal part is 12 1274616. The figure is shown in the figure. Figure 5 (b) is the insulation of the metal film remaining in the terminal part - Figure 6 is used to illustrate the second aspect of the present invention. Fig. 7 (4) and (b) are diagrams for explaining another aspect of the present invention in which metal film residue is prevented from occurring at the end portion. ^ 8th wire is used for illustration. A schematic diagram of an example of a device for removing a metal thin film according to the second aspect of the present invention is shown in Fig. 9. Fig. 9 is a view showing a gold-based film which remains in a punctiform shape at the end portion of the insulating material. In addition to the metal film of the third invention BRIEF DESCRIPTION OF THE DRAWINGS Fig. 11 is a schematic block diagram showing another example of a device for removing a metal thin film according to a third aspect of the present invention. Fig. 12 is a view showing another embodiment for carrying out the third invention. Fig. 13 is a schematic view showing an example of a device for removing the metal thin film of the fourth invention. Fig. 14 is a view showing the fourth embodiment. Fig. 15 is a schematic view showing a third example of a device for removing a metal thin film according to a fourth aspect of the invention. Fig. 16 is a view showing a schematic configuration of a second example of the apparatus for removing a metal thin film according to the fourth aspect of the invention. A schematic configuration diagram of a fourth example of the apparatus for removing a metal thin film according to the fourth aspect of the present invention is shown. Fig. 217461 shows a schematic configuration diagram of a fifth example of the apparatus for removing a metal thin film according to the fourth aspect of the present invention. Fig. 18 is an explanatory diagram of a method of removing a metal thin film by chemical etching (2) Component symbol 1 Chemical liquid 2 Substrate 21 Metal flat electrode 22 Auxiliary electrode 23 DC voltage power supply 24 Insulation 24a, 24b of metal film 25 processed groove 26a continuous flow of electrolyte 26 electrolyte solution tank 28 pump 27 filter 31 30 32 cylindrical conductive plate 34a of the insulator 33 made of rubber walls 34b rubber roller 35 spring

22 127461622 1274616

36 37 Μ V 絕緣物壁 電極 電解熔解析出部 閥36 37 Μ V Insulation wall Electrode Electrolytic melting analysis valve

23twenty three

Claims (1)

1274616 拾、申請專利範圍: 1 · 一種金屬薄骐之除去方法,其特徵在於:在對以傾 斜狀配置之金屬平板電極、以及辅助電極(位於此金屬平板 電極之上游側或下游側、以一部分會浸潰於電解液中所配 置者)施加直流電壓的狀態下,使得自該金屬平板電極上流 下之電解液與絕緣物表面之金屬薄膜衝撞,來將金屬薄膜 除去。 2·如申請專利範圍第1項之金屬薄膜之除去方法,其 中’在該絕緣物之背面側配置橫跨該金屬平板電極與辅助 電極間之底面電極,在此底面電極亦被施加與辅助電極呈 同極之直流電壓的狀態了,使得自該金屬平板電極上流下 之電解液與絕緣物表面之金屬薄膜衝撞,來將金屬薄膜除 3.如申睛專利範圍第! $ 2項之金屬薄膜之除去方法 ,其中,係在絕緣物與金屬平板電極做相對移動的同時 金屬薄膜除去。 4·如申請專利範圍第1 # 2項之金屬薄膜之除去方法 ’其中’在金屬平板電極之絕緣物進入侧設置抑制電解液 入侵構件’來抑制電解液之早期的入侵。 5.如申請專利範圍第3項之金屬薄膜之除去方法,其 中’在金屬平板電極之絕緣物進入側設置抑制電解液入; 構件,來抑制電解液之早期的入侵。 X 薄膜之除去方法 的電極,以在此 6.如申請專利範圍第丨或2項之金屬 ,其中,係將金屬平板電極做成旋轉自如 24 1274616 電極之金屬薄膜接觸部所設置之研磨基材來擦過金屬薄臈 之表面。 7·如申請專利範圍第4項之金屬薄膜之除去方法,其 中,係將金屬平板電極做成旋轉自如的電極,以在此電極 之金屬薄膜接觸部所設置之研磨基材來擦過金屬薄膜之表 面。 8·如申請專利範圍第5項之金屬薄膜之除去方法,其 中,係將金屬平板電極做成旋轉自如的電極,以在此電極 之金屬薄膜接觸部所設置之研磨基材來擦過金屬薄膜之表 面。 9·如申請專利範圍第3項之金屬薄膜之除去方法,其 中,係將金屬平板電極做成旋轉自如的電極,以在此電極 之金屬薄膜接觸部所設置之研磨基材來擦過金屬薄膜之表 面0 10.—種金屬薄膜之除去裝置,其特徵在於:係由 金屬平板電極,其呈傾斜狀配置,用以引導電解液之 流下; 輔助電極,其位於金屬平板電極之上游側或下游側, 以一部分會浸潰於電解液中所配置者;以及 直流電壓電源,其對前述兩電極施加電壓; 所構成者。 11·如申請專利範圍第10項之金屬薄膜之除去裝置, 係以橫跨金屬平板電極與輔助電極間的方式在此兩電極之 下方配置底面電極,此底面電極亦被直流電壓電源施加與 25 1274616 輔助電極呈同極之直流電壓。 12·如申請專利範圍第1〇或n項之金屬薄膜之除去裝 置,係設有一移動機構,可使得浸潰於電解液中之絕緣物 以及金屬平板電極中之至少一者相對於另一者做移動。 13. 如申請專利範圍第10或Π項之金屬薄膜之除去裝 置’係在金屬平板電極之絕緣物進入側設置抑制電解液入 侵構件。 14. 如申請專利範圍第12項之金屬薄膜之除去裝置, 係在金屬平板電極之絕緣物進入側設置抑制電解液入侵構 件。 15. 如申請專利範圍第10或n項之金屬薄膜之除去裝 置其中’係將金屬平板電極做成旋轉自如的電極,並在 此電極之金屬薄臈接觸部設置研磨基材、或是具備可對電 極之金屬薄膜接觸部供給研磨基材之供給機構。 16. 如申請專利範圍第12項之金屬薄膜之除去裝置, 其中’係將金屬平板電極做成旋轉自如的電極,並在此電 極之金屬薄膜接觸部設置研磨基材、或是具備可對電極之 金屬薄膜接觸部供給研磨基材之供給機構。 17·如申請專利範圍第13項之金屬薄膜之除去裝置, 其中,係將金屬平板電極做成旋轉自如的電極,並在此電 極之金屬薄膜接觸部設置研磨基材、或是具備可對電極之 金屬薄膜接觸部供給研磨基材之供給機構。 18.如申請專利範圍第14項之金屬薄膜之除去裳置, 其中’係將金屬平板電極做成旋轉自如的電極,並在此電 26 1274616 極之金屬薄膜接觸部設置研磨基材、或是具備可對電極之 金屬薄膜接觸部供給研磨基材之供給機構。 拾壹、圖式: 如次頁1274616 Pickup, Patent Application Range: 1 · A method for removing a thin metal crucible, characterized by: a pair of metal plate electrodes arranged in an inclined shape, and an auxiliary electrode (on the upstream side or the downstream side of the metal plate electrode, in part The electrolyte which flows down from the metal plate electrode collides with the metal film on the surface of the insulator to remove the metal thin film while being immersed in the electrolyte. 2. The method for removing a metal thin film according to claim 1, wherein 'the bottom surface electrode between the metal plate electrode and the auxiliary electrode is disposed on the back side of the insulator, and the bottom electrode is also applied to the auxiliary electrode The state of the DC voltage of the same pole is such that the electrolyte flowing down from the metal plate electrode collides with the metal film on the surface of the insulator to remove the metal film. A method of removing a metal film of $2, wherein the metal film is removed while the insulator and the metal plate electrode are relatively moved. 4. The method for removing a metal thin film according to the first and second aspects of the patent application section 'wherein' is provided with an electrolyte intrusion preventing member on the inlet side of the metal plate electrode to suppress early intrusion of the electrolytic solution. 5. The method of removing a metal thin film according to the third aspect of the patent application, wherein the member is placed on the insulating entry side of the metal flat electrode to suppress the intrusion of the electrolyte. The electrode of the method for removing the X film, which is the metal of the metal film connection of the electrode of the electrode of the 24 1274616 electrode, which is the metal of the metal film contact of the electrode of the 12 1274616 electrode. To wipe the surface of the thin metal. 7. The method for removing a metal thin film according to claim 4, wherein the metal flat electrode is made into a rotatable electrode, and the metal substrate is rubbed on the ground substrate provided at the metal film contact portion of the electrode. surface. 8. The method for removing a metal thin film according to claim 5, wherein the metal flat electrode is made into a rotatable electrode, and the metal substrate is rubbed on the ground substrate provided at the metal film contact portion of the electrode. surface. 9. The method for removing a metal thin film according to item 3 of the patent application, wherein the metal plate electrode is made into a rotatable electrode, and the metal substrate is rubbed by the abrasive substrate provided at the metal film contact portion of the electrode. Surface 0. 10. A metal film removing device, characterized in that it is composed of a metal plate electrode which is arranged in an inclined shape for guiding the flow of the electrolyte; and an auxiliary electrode which is located on the upstream side or the downstream side of the metal plate electrode. , a part of which is impregnated in the electrolyte; and a DC voltage source that applies a voltage to the two electrodes; 11. The apparatus for removing a metal thin film according to claim 10, wherein a bottom electrode is disposed below the two electrodes so as to be sandwiched between the metal plate electrode and the auxiliary electrode, and the bottom electrode is also applied by a DC voltage source. 1274616 The auxiliary electrode has a DC voltage of the same polarity. 12. The apparatus for removing a metal film according to the first or fourth aspect of the patent application is provided with a moving mechanism for causing at least one of the insulator impregnated in the electrolyte and the metal plate electrode to be relative to the other Do the move. 13. The metal film removing device of claim 10 or claim 3 is provided on the insulator entry side of the metal plate electrode to prevent the electrolyte intrusion member. 14. A metal film removing device according to claim 12, wherein the electrolyte intrusion member is provided on the insulating entry side of the metal plate electrode. 15. The apparatus for removing a metal thin film according to claim 10 or n wherein the metal plate electrode is made to be a rotatable electrode, and a polishing substrate is provided at the metal thin contact portion of the electrode, or A supply mechanism for the abrasive substrate is supplied to the metal film contact portion of the electrode. 16. The apparatus for removing a metal thin film according to claim 12, wherein the metal plate electrode is made to be a rotatable electrode, and a polishing substrate is provided at a contact portion of the metal film of the electrode, or a counter electrode is provided. The metal film contact portion supplies a supply mechanism for the polishing substrate. 17. The apparatus for removing a metal thin film according to claim 13 wherein the metal flat electrode is made of a rotatable electrode, and a polishing substrate is provided at a contact portion of the metal film of the electrode or a counter electrode is provided. The metal film contact portion supplies a supply mechanism for the polishing substrate. 18. The removal of the metal film according to claim 14 of the patent application, wherein the metal plate electrode is made into a rotatable electrode, and the polishing substrate is provided at the metal film contact portion of the electrode 26 1274616 or A supply mechanism that supplies a polishing substrate to the metal film contact portion of the electrode. Pick up, pattern: like the next page 2727
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JPS62290900A (en) * 1986-06-11 1987-12-17 Oki Electric Ind Co Ltd Method and apparatus for etching of transparent conductive film
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