TWI445844B - Electrode for electrolysis - Google Patents
Electrode for electrolysis Download PDFInfo
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- TWI445844B TWI445844B TW98141514A TW98141514A TWI445844B TW I445844 B TWI445844 B TW I445844B TW 98141514 A TW98141514 A TW 98141514A TW 98141514 A TW98141514 A TW 98141514A TW I445844 B TWI445844 B TW I445844B
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- TW
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- Prior art keywords
- electrode
- plate
- electrolysis
- base body
- power supply
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/10—Electrodes, e.g. composition, counter electrode
- C25D17/12—Shape or form
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D7/00—Electroplating characterised by the article coated
- C25D7/06—Wires; Strips; Foils
- C25D7/0614—Strips or foils
- C25D7/0635—In radial cells
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D7/00—Electroplating characterised by the article coated
- C25D7/06—Wires; Strips; Foils
- C25D7/0614—Strips or foils
- C25D7/0642—Anodes
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D1/00—Electroforming
- C25D1/04—Wires; Strips; Foils
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Electrolytic Production Of Metals (AREA)
- Battery Electrode And Active Subsutance (AREA)
Description
本發明係關於一種電解用電極,更詳細而言,為關於一種用於藉由電氣電鍍法製造電解銅箔等金屬箔之電解用電極。The present invention relates to an electrode for electrolysis, and more particularly to an electrode for electrolysis for producing a metal foil such as an electrolytic copper foil by an electroplating method.
在藉由電氣電鍍之金屬箔的製造中,近年來有電解裝置大電流化及大型化的傾向,就作為不溶性電極使用之電解用電極而言,能夠省空間化的曲面狀者習知以來就知道。例如在專利文獻1中,係揭示根據利用螺栓將陽極板安裝在殼體並使其彎撓而形成為圓弧狀的構成,將該圓弧狀的陽極板隔著間隔配置在可自由旋轉的圓筒型陰極周周,利用介在電解液,能夠在陰極表面析出金屬箔。又在陽極板與殼體之間介在接觸環,利用改變該接觸環的厚度,能夠調整陽極板與陰極之間隔。如此一來,能夠涵蓋整體將陽極板與陰極之間隔保持一定,使電流密度均勻化,而圖取析出的金屬薄膜之厚度均勻化。In the production of a metal foil by electroplating, in recent years, there has been a tendency for the electrolysis device to have a large current and an increase in size, and the electrode for electrolysis which is used as an insoluble electrode has been known to have a space-saving curved surface. know. For example, Patent Document 1 discloses a configuration in which an anode plate is attached to a casing by a bolt and bent in an arc shape, and the arc-shaped anode plate is rotatably disposed at intervals. On the circumference of the cylindrical cathode, a metal foil can be deposited on the surface of the cathode by interposing the electrolyte. Further, a contact ring is interposed between the anode plate and the casing, and the interval between the anode plate and the cathode can be adjusted by changing the thickness of the contact ring. In this way, the gap between the anode plate and the cathode can be kept constant to uniformize the current density, and the thickness of the deposited metal film can be made uniform.
但是,針對專利文獻1的構成,朝殼體之陽極板的安裝係由於根據從對殼體而言為與陽極板相反側插通螺栓加以進行,為了變更接觸環的厚度,因為在殼體外側必須進行螺栓的裝拆作業的同時,而且在殼體內側必須進行陽極板的裝拆作業,因此造成作業繁雜的問題。However, in the configuration of Patent Document 1, the mounting of the anode plate toward the casing is performed by inserting the bolt from the opposite side of the casing from the anode plate, in order to change the thickness of the contact ring, because it is outside the casing. At the same time that the bolts must be attached and detached, and the anode plate must be attached and detached inside the casing, the work is complicated.
為此,在專利文獻2中,係如第4圖所示,揭示在形成為圓弧狀的第1電極基體51內面側(與未圖示之陰極對向側)介由中間材52、53配置圓弧狀的第2電極基體54,利用螺栓從第1電極基體51內面側藉由螺栓55固定第2電極基體54之構成。如第5圖所示,第2電極基體54係為多數配置在第1電極基體51內周面,可以介由第1電極基體51從匯流條56對全部的第2電極基體54一體通電。根據專利文獻2,在進行中間材52、53的厚度調整之情況,可以只在第1電極基體51內面側進行中間材52、53的更換作業,而圖取作業性的提升。Therefore, in Patent Document 2, as shown in FIG. 4, the inner surface side (the opposite side to the cathode (not shown)) of the first electrode base 51 formed in an arc shape is interposed via the intermediate material 52, The arc-shaped second electrode base 54 is disposed, and the second electrode base 54 is fixed by bolts 55 from the inner surface side of the first electrode base 51 by bolts. As shown in FIG. 5, the second electrode base 54 is disposed on the inner circumferential surface of the first electrode base 51, and all of the second electrode bases 54 can be integrally supplied from the bus bar 56 via the first electrode base 51. According to Patent Document 2, when the thickness of the intermediate members 52 and 53 is adjusted, the replacement work of the intermediate members 52 and 53 can be performed only on the inner surface side of the first electrode base 51, and the workability can be improved.
然而,針對各個第1電極基體51而言要個別進行與陰極的間隔調整,仍然會殘留在作業面的問題,在該點中有進一步改良的空間。However, there is a problem that the first electrode base 51 is individually adjusted to be spaced apart from the cathode, and remains on the work surface, and there is room for further improvement.
(先前技術文獻)(previous technical literature)
(專利文獻)(Patent Literature)
[專利文獻1]日本特公平6-47758號公報[Patent Document 1] Japanese Patent Publication No. 6-47758
[專利文獻2]日本特開平8-209396號公報[Patent Document 2] Japanese Patent Laid-Open No. Hei 8-209396
因此,本發明係以提供易於使電解電流密度均勻化之電解用電極為目的。Therefore, the present invention has an object of providing an electrode for electrolysis which is easy to make the electrolytic current density uniform.
本發明之前述目的,係作為對可旋轉的陰極隔著間隔配置的陽極之電解用電極使用者,藉由具備:剖面圓弧狀的基體;及配置在該基體內面側的複數個電極板,構成為對前述各電極板能夠個別供電之電解用電極加以達成。The object of the present invention is to provide a substrate for electrolysis for an anode in which a rotatable cathode is spaced apart from each other, comprising: a base body having an arcuate cross section; and a plurality of electrode plates disposed on the inner surface side of the base body It is configured to achieve an electrolysis electrode that can individually supply power to each of the electrode plates.
針對該電解用電極,在前述基體與前述電極板之間介在絕緣性的彈性體為佳。It is preferable that the electrode for electrolysis has an insulating elastomer interposed between the base body and the electrode plate.
又前述電極板係可以構成為使朝外方突出的輪轂插通前述基體的貫穿孔,在與供電板之間介由絕緣性彈性體挾持前述基體,利用由前述供電板的外面側在前述輪轂的頭部螺鎖螺栓,而固定在前述基體。Further, the electrode plate may be configured such that a hub protruding outwardly is inserted through the through hole of the base body, and the base body is held between the power supply plate via an insulating elastic body, and the outer surface side of the power supply plate is on the hub The head bolts the bolts and is fixed to the aforementioned base body.
根據本發明,能夠提供易於使電解電流密度均勻化的電解用電極。According to the present invention, it is possible to provide an electrode for electrolysis which is easy to make the electrolysis current density uniform.
(用以實施發明之形態)(to implement the form of the invention)
以下,針對本發明之實施形態,參照添附圖面加以說明。第1圖為關於本發明一實施形態之電解用電極的剖面圖,並顯示用來作為電解槽的陽極之狀態。Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings. Fig. 1 is a cross-sectional view showing an electrode for electrolysis according to an embodiment of the present invention, and showing a state of being used as an anode of the electrolytic cell.
如第1圖所示,電解用電極1係形成為剖面圓弧狀,在本實施形態中,將2個電解用電極1、1配置為半圓狀,並兼作電解槽2的槽壁。在電解用電極1、1內側面係將可驅動旋轉的圓筒狀陰極4以順著圓周方向間隙大約一定的方式,隔著間隔加以配置。在電解槽2係介由設置在相鄰的2個電解用電極1、1間的供液部2a能夠供給電解液L,而被供給的電解液L係如箭頭所示方向通過電解用電極1、1與陰極4之間,並從設置在電解槽2的左右兩側之排出溝2b、2b朝外部排出。As shown in Fig. 1, the electrode for electrolysis 1 is formed in a circular arc shape. In the present embodiment, the two electrolysis electrodes 1 and 1 are arranged in a semicircular shape and also serve as a groove wall of the electrolytic cell 2. The cylindrical cathodes 4 that can be driven to rotate on the inner side surfaces of the electrodes 1 for electrolysis are arranged at intervals along the circumferential direction. In the electrolytic cell 2, the electrolytic solution L can be supplied through the liquid supply portion 2a provided between the adjacent two electrolysis electrodes 1 and 1, and the supplied electrolytic solution L passes through the electrolysis electrode 1 in the direction indicated by the arrow. Between 1 and the cathode 4, the discharge grooves 2b and 2b provided on the left and right sides of the electrolytic cell 2 are discharged to the outside.
第2圖為擴大顯示電解用電極1要部之剖面圖,第3圖為將其更加擴大顯示之剖面圖。如第2及3圖所示,電解用電極1係在剖面圓弧狀的基體10內側面(第1圖之與陰極4面對側)配置複數個同樣是剖面圓弧狀的電極板12加以構成。電極板12係使朝外方突出的輪轂12a插穿基體10的貫穿孔10a,並在電極板12與供電板16之間挾持基體10,藉由從供電板16外面側(第1圖之與陰極4的相反側)將螺栓18螺鎖在輪轂12a的頭部,而使電極板12固定在基體10。基體10係可以由例如鈦板加以構成,電極板12係可以成為例如利用氧化銥等塗佈鈦板內面側之不溶性電極。Fig. 2 is a cross-sectional view showing an enlarged main portion of the electrode 1 for electrolysis, and Fig. 3 is a cross-sectional view showing the enlarged portion of the electrode. As shown in Figs. 2 and 3, the electrode for electrolysis 1 is provided with a plurality of electrode plates 12 having the same arc shape in cross section on the inner side surface of the base body 10 having an arcuate cross section (the side facing the cathode 4 in Fig. 1). Composition. The electrode plate 12 is such that the hub 12a protruding outwardly is inserted through the through hole 10a of the base 10, and the base 10 is held between the electrode plate 12 and the power supply plate 16 by the outer side of the power supply plate 16 (Fig. 1) The opposite side of the cathode 4 is screwed to the head of the hub 12a to fix the electrode plate 12 to the base 10. The base 10 can be formed, for example, of a titanium plate, and the electrode plate 12 can be, for example, an insoluble electrode on the inner surface side of the titanium plate coated with ruthenium oxide or the like.
在電極板12與基體10之間、以及在基體10與供電板16之間係介在形成為環狀的橡膠材料等具有絕緣性的彈性體20、22。Insulating elastomers 20 and 22, such as a rubber material formed in a ring shape, are interposed between the electrode plate 12 and the base 10 and between the base 10 and the power supply plate 16.
各電極板12係以覆蓋基體10的內面整體之方式整列配置,在各個之間則確保絕緣用的間隙S。在各電極板12係介由連接在供電板16之由單芯電線構成的配線16a,能夠朝箭頭所示方向供給電流,構成為可以個別供電。Each of the electrode plates 12 is arranged in a line so as to cover the entire inner surface of the base 10, and a gap S for insulation is secured between the electrodes. Each of the electrode plates 12 is supplied with a current in a direction indicated by an arrow via a wiring 16a composed of a single-core electric wire connected to the power supply plate 16, and is configured to be individually powerable.
根據具有上述構成之電解用電極1,在各電極板12與陰極4的電極間距離產生偏差而使電流密度不均勻的疑慮之情況,不是如習知所示調整電極間距離,而是可以個別調整供電至各電極板12的電流值。具體而言,藉由在測定的電極間距離為小時將供電電流值變大,一方面在電極間距離為大時將供電電流值變小,能夠使陰極的電流密度分布均勻化,並且只要利用供電電流值的調整,就能夠易於使析出金屬的厚度均勻化。電極間距離與供電電流值係如上述所示,由於有相反比例的關係,因此藉由將對應電極間距離的供電電流值預先表格化或數式化,可以更易於決定每個電極板12的供電電流值。According to the electrode for electrolysis 1 having the above-described configuration, when the distance between the electrodes of the electrode plates 12 and the cathode 4 varies, and the current density is not uniform, the distance between the electrodes is not adjusted as shown in the prior art, but may be individually The current value supplied to each electrode plate 12 is adjusted. Specifically, when the distance between the electrodes measured is small, the supply current value is increased, and when the distance between the electrodes is large, the supply current value is made small, and the current density distribution of the cathode can be made uniform, and only By adjusting the value of the supply current, it is possible to easily make the thickness of the precipitated metal uniform. The distance between the electrodes and the value of the supply current are as described above. Since there is an inverse proportional relationship, it is easier to determine the shape of each electrode plate 12 by pre-tableting or digitizing the value of the supply current corresponding to the distance between the electrodes. Supply current value.
又利用在基體10與電極板12之間介在絕緣性彈性體20之狀態,由於電極板12為固定在基體10,因此能夠確定防止貯留在電解槽2之電解液L的漏出,而且能夠確保基體10與電極板12之間的電氣絕緣。Further, in the state in which the insulating elastic body 20 is interposed between the base 10 and the electrode plate 12, since the electrode plate 12 is fixed to the base 10, it is possible to secure leakage prevention of the electrolytic solution L stored in the electrolytic cell 2, and to secure the substrate. Electrical insulation between 10 and electrode plate 12.
再者,藉由在基體10與供電板16之間也介在彈性體22,可以達介由供電板16之對電極板12的穩定供電,藉由供電電流值的調整可以確實控制電流密度。Furthermore, by interposing the elastomer 22 between the substrate 10 and the power supply board 16, stable power supply to the counter electrode plate 12 of the power supply board 16 can be achieved, and the current density can be surely controlled by adjusting the supply current value.
1...電解用電極1. . . Electrolytic electrode
10...基體10. . . Matrix
10a...貫穿孔10a. . . Through hole
12...電極板12. . . Electrode plate
12a...輪轂12a. . . Wheel hub
16...供電板16. . . Power supply board
18...螺栓18. . . bolt
20、22...彈性體20, 22. . . Elastomer
第1圖係為關於本發明一實施形態之電解用電極的剖面圖。Fig. 1 is a cross-sectional view showing an electrode for electrolysis according to an embodiment of the present invention.
第2圖係為擴大顯示第1圖所示之電解用電極要部的剖面圖。Fig. 2 is a cross-sectional view showing an enlarged main portion of the electrode for electrolysis shown in Fig. 1 .
第3圖係為更擴大顯示第1圖所示之電解用電極要部的剖面圖。Fig. 3 is a cross-sectional view showing the main part of the electrode for electrolysis shown in Fig. 1 in an enlarged manner.
第4圖係為習知電解電極的要部剖面圖。Fig. 4 is a cross-sectional view of a principal part of a conventional electrolytic electrode.
第5圖係為顯示第4圖所示之電解用電極的整體構成之立體圖。Fig. 5 is a perspective view showing the overall configuration of an electrode for electrolysis shown in Fig. 4.
10...基體10. . . Matrix
12...電極板12. . . Electrode plate
16...供電板16. . . Power supply board
S...間隙S. . . gap
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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JP2008311801A JP5414257B2 (en) | 2008-12-08 | 2008-12-08 | Electrode for electrolysis |
Publications (2)
Publication Number | Publication Date |
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TW201035381A TW201035381A (en) | 2010-10-01 |
TWI445844B true TWI445844B (en) | 2014-07-21 |
Family
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TW98141514A TWI445844B (en) | 2008-12-08 | 2009-12-04 | Electrode for electrolysis |
Country Status (4)
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JP (1) | JP5414257B2 (en) |
CN (1) | CN102239281B (en) |
TW (1) | TWI445844B (en) |
WO (1) | WO2010067754A1 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2013030870A1 (en) * | 2011-08-30 | 2013-03-07 | 西工業株式会社 | Metal foil electrolytic deposition device |
JP6946911B2 (en) | 2017-09-29 | 2021-10-13 | 株式会社大阪ソーダ | Manufacturing equipment for plating electrodes and electrolytic metal leaf |
CN107916441B (en) * | 2017-11-08 | 2019-08-09 | 铜陵市宏达家电有限责任公司 | A kind of tow sides non-bolt anode of Electrolytic copper foil generator |
KR102528177B1 (en) * | 2019-03-21 | 2023-05-02 | 에스케이넥실리스 주식회사 | Apparatus for Electrodeposition of Electrolytic Copper Foil and Apparatus for Manufacturing of Electrolytic Copper Foil |
CN113174616B (en) * | 2021-04-28 | 2022-02-25 | 广东嘉元科技股份有限公司 | Improved generation electrolytic copper foil production facility of current adjustable |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH0436493A (en) * | 1990-05-31 | 1992-02-06 | Nikko Guurudo Foil Kk | Device for producing electrolytic copper foil |
JP2506574B2 (en) * | 1990-12-19 | 1996-06-12 | 日鉱グールド・フォイル株式会社 | Method and apparatus for producing electrolytic copper foil |
US5326455A (en) * | 1990-12-19 | 1994-07-05 | Nikko Gould Foil Co., Ltd. | Method of producing electrolytic copper foil and apparatus for producing same |
TW197534B (en) * | 1991-03-21 | 1993-01-01 | Eltech Systems Corp | |
JPH0610185A (en) * | 1992-06-24 | 1994-01-18 | Nippon Steel Corp | Electroplating device for metallic strip |
JP4439081B2 (en) * | 2000-05-31 | 2010-03-24 | 日本電解株式会社 | Electrolytic copper foil manufacturing method and apparatus used therefor |
-
2008
- 2008-12-08 JP JP2008311801A patent/JP5414257B2/en not_active Expired - Fee Related
-
2009
- 2009-12-03 WO PCT/JP2009/070340 patent/WO2010067754A1/en active Application Filing
- 2009-12-03 CN CN200980149105.0A patent/CN102239281B/en not_active Expired - Fee Related
- 2009-12-04 TW TW98141514A patent/TWI445844B/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
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CN102239281A (en) | 2011-11-09 |
JP2010132993A (en) | 2010-06-17 |
CN102239281B (en) | 2014-08-20 |
TW201035381A (en) | 2010-10-01 |
JP5414257B2 (en) | 2014-02-12 |
WO2010067754A1 (en) | 2010-06-17 |
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