EP0504939A2 - Elektrolytische Zelle-Anode - Google Patents

Elektrolytische Zelle-Anode Download PDF

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Publication number
EP0504939A2
EP0504939A2 EP92104923A EP92104923A EP0504939A2 EP 0504939 A2 EP0504939 A2 EP 0504939A2 EP 92104923 A EP92104923 A EP 92104923A EP 92104923 A EP92104923 A EP 92104923A EP 0504939 A2 EP0504939 A2 EP 0504939A2
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EP
European Patent Office
Prior art keywords
anode
cell
cathode
strips
configuration
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP92104923A
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English (en)
French (fr)
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EP0504939A3 (en
EP0504939B1 (de
Inventor
Gerald R. Pohto
Zane A. Wade
H. Kirk Fowler
Andrew J. Niksa
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Eltech Systems Corp
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Eltech Systems Corp
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Publication date
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Publication of EP0504939A3 publication Critical patent/EP0504939A3/en
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    • 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
    • C25D17/06—Suspending or supporting devices for articles to be coated
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C7/00—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
    • 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

Definitions

  • the present invention relates to anodes for electrolytic cells, for such applications as electroplating, electrowinning, electrofinishing and electromachining, and particularly to anodes having a dimensionally stable active anode surface.
  • dimensionally stable electrodes are well known.
  • the term "dimensionally stable" means that the electrodes are not consumed during use.
  • a dimensionally stable electrode comprises a substrate and a coating on surfaces of the substrate.
  • the substrate and coating have to withstand the corrosive action of the electrolyte in which the electrode is immersed.
  • One suitable material for the substrate is a valve metal, such as titanium, tantalum, zirconium, aluminum, niobium and tungsten. These metals are resistant to electrolytes and to conditions used within electrolytic cells.
  • a preferred valve metal is titanium.
  • the valve metals can become oxidized on their surfaces increasing the resistance of the valve metals to the passage of current. Therefore, it is customary to apply electrically conductive, electrocatalytic coatings to the electrode substrate.
  • the coatings have the capacity to continue to conduct current to the electrolyte over long periods of time without becoming passivated.
  • Such coatings can contain catalytic metals or oxides from the platinum group metals such as platinum, palladium, iridium, ruthenium, rhodium and osmium.
  • the anode for an electrolytic cell such as an electrowinning cell is usually in the shape of a large surface which conforms generally to the shape of the cell cathode, but is spaced from the cathode.
  • the cathode in which the cathode is in the shape of a relatively large, cylindrical drum, rotatable on the axis of the drum, the anode will have a cylindrically shaped concentric surface circumferentially superimposed over a relatively large part of the cathode.
  • valve metals are resilient, and are difficult to roll to a predetermined curvature with close tolerance. Coating the valve metals further exaggerates the problem, since the coatings have to be heat treated, and the heat treatment can cause further deviation of the anodes from a desired curvature.
  • U.S. Patent No. 4,318,794 discloses a radial electrolytic cell for metal winning.
  • a plurality of dimensionally stable, elongated, anode strips are positioned in the cell electrolyte spaced from a cylindrical cathode.
  • the anode strips extend, longitudinally, parallel to the axis of the cathode.
  • Each strip is relatively narrow in width, being co-extensive, circumferentially, with only a small surface or arc of the cathode.
  • the tolerances to which each strip is rolled become less critical.
  • the strips are about 2-4 inches in width.
  • U.S. Patent No. 4,642,173 discloses an electroplating cell.
  • the cell comprises a dimensionally stable anode for depositing metal onto an elongated strip drawn longitudinally past the anode.
  • the anode is immersed in an electrolytic solution and comprises an active surface which is directed toward the strip.
  • the active surface comprises a plurality of lamellas supported so that all of the lamellas lie in a boundary which conforms to but is spaced from the path of the strip.
  • Each lamella is welded to a support, along an edge, with the opposite edge of the lamella facing the strip. Being welded to a support, the lamellas are not readily replaceable. In addition, they are spaced apart from each other and thus do not present a continuous or substantially continuous anode surface.
  • the present invention relates to an electrolytic cell which comprises a cathode having a cathode surface movable in said cell, an anode spaced from said cathode, and means for maintaining an electrolyte solution between the cathode and the anode.
  • the anode comprises at least one dimensionally stable elongated anode strip at right angles to the cathode surface direction of movement.
  • the anode strip is laterally flexible and has a formed, first configuration.
  • a support means supports the anode strip and flexes the anode strip into a second supported configuration which is different from the formed first configuration.
  • the anode strip in the second supported configuration is essentially uniformly spaced from the cathode. In a radial cell, the anode is flexed into a configuration, which, in cross-section, at right angles to the longitudinal dimension of the anode, is arcuate.
  • the present invention also resides, in one embodiment, in a novel anode configuration.
  • the anode is dimensionally stable in an electrolyte.
  • the anode is in the shape of an elongated channel having an active anode surface, and longitudinally extending flanges along opposite side edges of the active anode surface.
  • the active anode surface has a thickness by which it is flexible. Supports engage the anode flanges so as to flex the active anode surface from a formed, first configuration, into a second supported configuration which is different from the formed, first configuration and which positions the active anode surface uniformly spaced from the cathode.
  • the electrolytic cell comprises a plurality of elongated anodes positioned in side-by-side relationship, in an arc or plane, uniformly spaced from the cathode.
  • the present invention is useful for an electrolytic cell in which the anode defines an essentially continuous surface and the electrolyte flow is confined to a path defined by the anode and the cathode.
  • the present invention is also useful for an electrolytic cell in which the anode is immersed in the electrolyte contained within the cell.
  • the electrolytic cells of the present invention are particularly useful in an electroplating process in which a deposit of a metal, such as zinc, is made onto a moving cathode strip.
  • a deposit of a metal such as zinc
  • An example of such a process is electrogalvanizing in which zinc is continuously galvanized onto a strip fed from a steel coil.
  • the electrolytic cells of the present invention can also be used in other electrodeposition processes, for instance plating other metals such as cadmium, nickel, tin and metal alloys such as nickel-zinc, onto a substrate, or the production of electrodeposited foil, for instance, copper foil used in the production of printed circuits for electronic and electrical equipment.
  • the copper foil is electrodeposited from an electrolyte onto the surface of a rotating cathode. The foil emerges from the electrolyte and is stripped from the surface of the cathode, and is wound in the form of a coil onto a roll, all in a known manner.
  • Another electrodeposition process is surface treating foil, for instance copper foil, previously manufactured. Copper foil, when used for printed circuit boards, is bonded to a dielectric substrate. Electrodeposited copper foil has poor adhesion properties, because of its relatively smooth surfaces. It is conventional practice to surface treat the copper foil to obtain improved mechanical bonding properties between the substrate and the foil.
  • One such treatment comprises forming a layer of dendritic copper or copper oxide particles on the surface of the foil.
  • Another such treatment comprises forming a locking layer over the dendritic layer which adopts the configuration of the dendritic surface but helps maintain the dendritic layer intact.
  • the cell of the present invention can be also used in non-plating processes such as electromachining, electrofinishing, anodizing, electrophoresis, and electropickling.
  • the anode of the electrolytic cell of the present invention can also be used in such applications as batteries and fuel cells, and in such processes as the electrolytic manufacture of chlorine and caustic soda.
  • the gap between the anode and the cathode it is necessary to carefully adjust the gap between the anode and the cathode. For instance, in electroplating, this in part controls the thickness of the layer which is electroplated. In the manufacture of electrodeposited foil, this in part controls the thickness of the foil.
  • the present invention is concerned primarily with control of the anode/cathode gap.
  • the vessel 10 encompasses a cylindrical cathode 12, shown in phantom lines in Fig. 2.
  • the vessel 10 has a concave shell 14 which is supported by end stanchions 16, 18.
  • the shell 14 defines a chamber 20 which receives the cathode 12.
  • the shell 14 is closed at its ends by circular end plates 22, 24 which are bolted to the stanchions 16, 18.
  • the end plates 22, 24 support pillow blocks 26, 28 which in turn support the cylindrical cathode 12 when the electrodeposition apparatus is completely assembled.
  • the cylindrical cathode 12 has an axial supporting shaft which is rotatably mounted in the pillow blocks 26, 28, in a known manner.
  • the pillow blocks 26, 28 are positioned on the end plates 22, 24 so that the cathode is partially encompassed by the shell 14.
  • the vessel shell 14 and end plates 22, 24 therefor are preferably made of a current-conductive metal, having high tensile strength, such as steel and copper.
  • the cylindrical cathode 12 can be of any conventional type.
  • the cathode is a metal, e.g., steel or copper, drum having a surface layer suitable for use in an electrolytic bath.
  • suitable metals for the surface layer are "Hastelloy” (trademark Union Carbide Corp., for a high strength, nickel-base corrosion resistance alloy) stainless steel, titanium, zirconium and tantalum.
  • shell 14 is shown as substantially a semi-circle, other shell configurations can be used.
  • the shell can be made so that it extends circumferentially a distance more than 180° around the cathode 12, for instance 260°.
  • the shell 14 will be circular so that all surfaces of the shell 14 are equidistantly spaced from the cathode 12 which is contained by the shell.
  • the end plates 22, 24 on the shell are removable. This permits the cathode to be inserted into the shell endwise rather than from the top. This mode of assembly is particularly useful if the shell 14 circumscribes the cathode by more than 180°.
  • a thin film of metal is deposited from electrolyte in the shell 14 onto the surface of rotating cathode 12.
  • the shell 14 is lined on its inner surface with a plurality of elongated anode plates 32. Details of the anode plates 32 are shown in Fig. 6. Essentially, the anode plates 32 are elongated rectangular members having ends 34, 36, side edges 38, 40 and an active anode surface 42. The anode plates are bolted to the shell 14, in a manner to be described. As shown in Figs. 1, 2 and 4, the entire inner surface of shell 14 is lined with anode plates 32. The anode plates are positioned so that the edges 38, 40, Fig. 6, of one plate are contiguous with edges 38, 40 of adjacent plates.
  • all of the anode plates together lie in an arc which is coaxial with the axis of the cathode and spaced from the surface of the cathode, the arc embracing, in the example of Figs. 1-9, about 180° of the circumference of the cathode.
  • the anode plates 32 are dimensionally stable electrodes.
  • the dimensionally stable electrodes have a substrate which is capable of withstanding the corrosive action of the electrolyte in which the anode plates are immersed.
  • Preferred materials for the substrate are a valve metal such as titanium, tantalum, zirconium, aluminum, niobium, and tungsten. These metals are resistant to electrolytes and conditions within an electrolytic cell.
  • a preferred valve metal is titanium.
  • valve metals can become oxidized on their surfaces increasing the resistance of the valve metal to the passage of current, thereby passivating the anodes. Therefore, it is customary to apply electrically conductive electrocatalytic coatings to the substrate which do not become passivated.
  • Such coatings can contain catalytic metals or oxides from the platinum group metals such as platinum, palladium, iridium, ruthenium, rhodium and osmium.
  • the coating also preferably contains a binding or protective agent such as oxides of titanium or tantalum, or other valve metal, in sufficient amount to bind the platinum group metal or oxide to the electrode substrate.
  • An example of one such dimensionally stable anode is a titanium substrate which has been coated with an electrocatalytic coating containing ruthenium and titanium.
  • the substrate can also be a metal such as steel or copper which is explosively clad or plated with a valve metal, such as titanium, and then coated with an active oxide surface.
  • a metal such as steel or copper which is explosively clad or plated with a valve metal, such as titanium, and then coated with an active oxide surface.
  • the anode plates 32 are thin gauge, resilient, rolled, or otherwise formed plates having sufficient flexibility so that they can be flexed a small amount using reasonable bolting force.
  • the plates 32 should have sufficient thickness to carry current from a current connection throughout the anode active surface, and sufficient thickness so that the plates are self-supporting and capable of retaining, in the absence of applied force, the shape imparted to them by rolling or other forming.
  • the anode plates 32 have a thickness of about 0.010 inch to about 0.5 inch.
  • a thin coated titanium plate rolled, or otherwise formed, preferably has a thickness of about 0.20 to about 0.25 inch. The thinner the plate, the easier it is to install, and the lower the material cost.
  • the specific width dimension of the anode plates 32, between side edges 38, 40, is not critical. In the example illustrated in Fig. 6, the anode plates are relatively wide, about twenty-four inches.
  • each anode plate 32 can comprise several end-to-end segments 32a, 32b and 32c, Fig. 6, positioned longitudinally within the shell 14.
  • the segments are separated by lines of separation 44 that are biased, e.g., biased with respect to the direction of travel of a metal film electrodeposited on cathode 12. This avoids unevenness of the electrodeposition of metal due to edge effects.
  • the anode plates 32 from end 34 to end 36 can be relatively long, and dividing the anode plates into segments 32a, 32b and 32c facilitates forming and installation.
  • Fig. 7 shows the method of attachment of the anode plates 32 to the shell 14, and additional details of the vessel 10.
  • the vessel shell 14 has an inner lining 58.
  • the lining 58 covers the entire inner surface of shell 14, and lies between the plurality of anode plates 32 and the shell 14.
  • the lining 58 can be any suitable lining material for an electrolytic cell.
  • the lining has a high durometer hardness, for instance a Shore durometer of about 95 ⁇ 5, and is machinable.
  • the lining 58 is baked onto the inner surface of the shell 14.
  • One suitable lining material is manufactured natural rubber.
  • Other suitable materials are neoprene and EPDM (a terpolymer elastomer made from ethylene-propylene diene monomer).
  • the purpose of lining 58 is to protect the shell 14 from corrosion by the electrolyte.
  • the bosses 62 are shown in Fig. 6 in phantom lines.
  • the bosses 62 are shown all aligned on the center-line of the anode plates.
  • the bosses 62 are made of a valve metal, such as titanium.
  • the bosses 62 are drilled and internally threaded.
  • Bolts 64 extend through holes 66, in shell 14, aligned with bosses 62 and are threaded into the bosses 62 to secure the anode plates 32 to the shell 14.
  • the bolts 64 can be made of steel or copper alloy, and preferably are coated with a dielectric, electrolyte resistant coating such as Teflon (trademark, E. I. DuPont de Nemours & Co.) for corrosion and galling resistance.
  • Teflon trademark, E. I. DuPont de Nemours & Co.
  • the lining 58 has openings 68 aligned with holes 66 adapted to receive bosses 62.
  • the shell 14 is undercut on the inside at 70 to receive the bosses 62.
  • the lining 58 is undercut at 72 to receive O-ring seals 74.
  • seals 74 One suitable seal material, for seals 74, is Viton (Trademark, E. I. DuPont de Nemours & Co.), a fluoroelastomer based on the copolymer of vinylidene fluoride and hexafluoropropylene.
  • Viton Trademark, E. I. DuPont de Nemours & Co.
  • the O-ring seals 74 bear against the underside 60 of the anode plate 32 and prevent leakage of electrolyte from the interior of vessel 10 around the bolts 64.
  • the current flow to the anode plates 32 is from shell 14 through the anode bosses 62. These anode bosses bear against a contact ring 76 seated at the bottom of undercut 70.
  • the contact ring conveys current from the shell 14 to the anode bosses 62.
  • the ring can be a knurled copper ring, or a compression ring such as shown in Fig. 7a.
  • the contact ring 76 comprises a copper alloy strip 78.
  • the copper alloy strip 78 is wound in the shape of a spring coil, and has a chevron cross-section, as shown.
  • a fiber reinforced polymeric or rubber filling 80 is positioned between rolls of the copper strip 78.
  • the anode plates 32 are sealed at their edges 38, 40 by means of support strips 90.
  • the support strips 90 are inserted into parallel grooves 92 machined into the exposed surface of the lining 58.
  • the grooves 92 retain the support strips 90.
  • the support strips 90 have a thickness whereby they protrude slightly above the exposed surface of lining 58.
  • the opposed edges 38, 40 of adjacent anode plates 32 seat on the exposed surfaces of the support strips 90.
  • the support strips 90 can be titanium strips or fiberglass. They are incompressible and thus are load bearing.
  • the support strips 90 extend, longitudinally, coextensive with the anode plates 32, between the end plates 22, 24 of the electrodeposition apparatus, sealing the opposed edges 38, 40 of adjacent anode plates 32 the full distance between the end plates 22, 24.
  • the end plates 22, 24 are also lined, on their inner surfaces, with a lining (not shown), similar to the shell lining 58. This seals the anodes 32, at their ends 34, 36 (Fig. 6), thereby sealing the vessel 10 against the leakage of electrolyte. Similar sealing can be employed at bias cuts 44, if the same are used.
  • the method of assembling the anode plates 32 into the electrodeposition apparatus in accordance with the present invention will be apparent, by reference to Figs. 8a, 8, and 7.
  • the anode plates 32 are rolled to a flat, or near flat configuration, as shown by the solid lines in Fig. 8a. It is understood that the anode plates can be rolled to a convex configuration or a concave configuration, depending upon the end configuration desired for the anode plates.
  • the anode plates 32 are then placed in the shell 14, with the bosses 62 aligned with bolts 64 (Fig. 7). The bolts 64 are engaged with the bosses 62.
  • the side edges 38, 40 of the anode plate 32 bear against the edge support strips 90, on the inner side of the lining 58 (Fig. 8).
  • the bolts 64 are turned into bosses 62. This pulls the bosses 62 toward the shell 14 flexing the anode plate 32 into the configuration shown in dashed lines in Fig. 8a.
  • the anode plates 32 at bosses 62 are against or contiguous with contact rings 76 (Fig. 7)
  • the anode plates 32 have the desired configuration, e.g., the same configuration as the shell 14.
  • the anode plates 32 are spaced from lining 58 by a gap 98. It will be apparent that this gap, or the radial distance of the anode plates 32 from the axis of the cathode 12, can be varied by changing the radial dimensions of support strips 90 and contact rings 76 (Figs. 8 and 7, respectively). In addition, the configuration or arc prescribed by an anode plate 32, as shown in the dashed lines of Fig. 8a, can be varied by changing the radial dimension of either the contact ring 76 or the support strip 90.
  • the shell 14 has at its bottom an orifice plate 48.
  • the orifice plate 48 is fastened to the underside of the shell 14. Details of the orifice plate 48 are disclosed in Fig. 9.
  • the orifice plate 48 has a plenum chamber 50 and an inlet connection 52 for introducing electrolyte into the plenum chamber 50.
  • the plenum chamber 50 is open at its top in elongated orifice 54 through which electrolyte flows into the shell 14 and into the electrolyte chamber 84, between the cathode 20 and anode plates 32.
  • the anode plates 32 have at their edges 38, 40, embracing the orifice plate 48, support strips 90, sealing the anode plates 32 against leakage of electrolyte between the plates and shell lining 58.
  • the support strips 90 are the same as those shown in Fig. 8.
  • the flow of electrolyte into the electrodeposition apparatus is into the inlet 52 (Fig. 9), into plenum chamber 50 at the bottom of the cell, through orifice 54, and into the interior of the vessel 10. Since the anode plates are fully sealed, along edges 38, 40, and around bosses 62, the anode plates 32, with the cathode 12, define the annular electrolyte chamber 84 (Figs. 2 and 9) through which the electrolyte flows.
  • the electrodeposition apparatus comprises an upper housing 82.
  • the housing 82 has discharge plenums 86 along opposite sides. Each plenum 86 has a plurality of discharge ports 88.
  • the electrolyte flows upwardly along both sides of the cathode 12, spilling out over edges of the discharge plenums 86 exiting in discharge ports 88.
  • the current flow in the electrodeposition apparatus is established by busses 96 affixed to end stanchions 16, 18 of the cell and ribs 94 (Fig. 1). Only two such busses are shown, in Figs. 2 and 3.
  • the flow from the end stanchions and ribs is through the shell 14, contact rings 76 (Fig. 7), and bosses 62 into the anode plates 32.
  • the flow of current is then through the electrolyte, through the cathode, and typically to conventional cathode brushes engaging the cathode support shaft in a known manner.
  • the apparatus of Figs. 1-9 can be characterized as a contained-flow apparatus, in which the flow of electrolyte is confined between the anode plates 32 and the cathode. Wiper seals (not shown) between the end plates 22, 24 and the cathode 12 prevent the cathode from being immersed in electrolyte except at the cathode active surface facing anode plates 32. It will be understood that the anode support structure disclosed can also be used in the type of cell in which the anodes are immersed in the electrolyte.
  • the electrodeposition apparatus comprises a tank 102.
  • the tank 102 is rectangular in cross section, having bottom 104, and sides 106, 108.
  • the tank is open at its top between sides 106, 108.
  • the tank 102 is filled with a suitable electrolyte (not shown).
  • a rotatable cylindrical cathode 110 shown in phantom lines, is positioned within the tank 102 so as to be partially immersed in the electrolyte.
  • the cell of Figs. 10-13 can be characterized as a flooded design, in which the anode and part of the cathode are immersed in the electrolyte.
  • the beams 112 are supported by the tank end walls 114 (Fig. 11).
  • the beams 112 in turn support a plurality of spaced apart supporting ribs 116, 118 (Figs. 10 and 11).
  • Fig. 11 is a section view of Fig. 10, taken so that the side 106 of the tank is removed, revealing the inside of the tank.
  • the ribs 116 are end ribs positioned near end walls 114 of tank 102
  • the ribs 118 are inner ribs, positioned at spaced intervals between the ribs 116.
  • the end ribs 116 are supported by inner beams 112a (Fig. 10), and the inner ribs 118 are supported by all of the beams 112 (Fig. 10).
  • the ribs 116, 118 are arrayed in sets divided by gap 120, one set of ribs being arrayed along one side 106 of the tank 102, the other set of ribs being arrayed along the other side 108 of tank 102.
  • Each rib 116, 118 along one side of tank 102 has a corresponding rib oppositely positioned along the other side of the tank.
  • Each rib has a concave upper edge 122, a lower edge 124 which seats on a beam 112, and a vertical edge 126.
  • the concave edge 122 of one rib faces the concave edge 122 of an oppositely positioned rib so that a pair of ribs together define, by the concave edges 122, a circular configuration as shown in Fig. 10.
  • the circular configuration is concentric with the circumference of cathode 110, although this is not essential.
  • the concave edges 122 of the ribs along one side 106 of the tank are all aligned lengthwise in the tank, and, similarly, the concave edges 122 of the ribs along the side 108 of the tank are all aligned lengthwise in the tank. This also is not critical, and other configurations for the ribs will be apparent to those skilled in the art.
  • the ribs are tied together by tie plates 128 welded to the vertical edges 126 of the ribs. Similar tie plates 128 are welded to the lower edges 124 of the ribs.
  • the tie plates 128 extend lengthwise in the apparatus, parallel to beams 112, and are welded to all of the ribs 116, 118. This permits the ribs 116, 118 and other components of the electrodeposition apparatus to be preassembled outside of the tank 102, and then set in the tank onto beams 112, as a preassembly.
  • the electrodeposition apparatus of Figs. 10 and 11 comprises a plurality of anode plates 130, shown in Figs. 10a and 12.
  • the anode plates 130 are positioned circumferentially around the cathode 110, generally concentric with the outer surface of the cathode, similar to anode plates 32 of the embodiment of Figs. 1-9.
  • the anode plates 130 are dimensionally stable, as with the anode plates of the embodiment of Figs. 1-9.
  • the anode plates 130 are rolled as U-shaped channels 132 as shown in Fig. 10a.
  • Each channel 132 comprises an elongated rectangular center portion 134 and longitudinally extending edge flanges 136, 138.
  • the edge flanges 136, 138 are angled, for instance at generally right angles, with respect to the center portion 134.
  • the center portion 134, between edge flanges 136, 138 is relatively wide, for instance about 12-24 inches.
  • the center portion has on one side 142, Fig. 10a, an active anode surface which, as will be described, faces cathode 110. Only the active anode surface and flanges 136, 138 are coated with a non-passivating coating.
  • the anode plates 130 are rolled or otherwise formed so that the center portion 134 adopts an essentially flat configuration, as shown by the solid lines in Fig. 10a.
  • the channels 132 can be rolled or otherwise formed to a concave or convex configuration, depending upon the end configuration of the anode plates which is desired.
  • the flanges 136, 138 of adjacent anodes are bolted together by bolts 140.
  • the bolts 140 hold the outer face of one flange 136, of one anode plate 130, against the outer face of another flange 138, of another anode plate 130. In this way, the bolts 130 connect and hold together the entire array of side-by-side anode plates.
  • the number of bolts 140, holding one anode plate to another, is sufficient to maintain an essentially uniform contact, lengthwise of each plate, between the connected flanges of adjacent plates.
  • the anode plates 130 are supported, at each bolt 140, by a bracket assembly 150 (Figs. 12 and 13).
  • Each bracket assembly 150 comprises a current distribution bar 152, which extends the full length of the electrodeposition apparatus. Six such distribution bar 152 are shown in Fig. 11.
  • the distribution bars 152 are affixed, e.g., welded, along one edge 152a (Figs. 12 and 13), to an adjustment clip 154.
  • Each adjustment clip 154 is bolted to a cell rib 116, 118 by a bolt 156.
  • the adjustment clips are positioned close to concave edges 122 of the ribs 116, 118.
  • Each adjustment clip 154 has a slot 158 (Fig. 12).
  • the adjustment clips 154 are movable circumferentially, on ribs 116, 118, by engagement of slots 158 with bolts 156. This permits circumferential adjustment of each anode plate 130 with respect to cathode 112.
  • a jack screw 162 is welded to each rib and engages clip 154. The bolts 156 can be partially tightened on the clips 154. The jack screws 162 can then be turned forcing the clips 154 into a desired circumferential position. This permits fine positioning of the anode plates. The bolts 156 can then be fully tightened on the clips 154 securely holding the anode plates 112 to the ribs.
  • the distributor bars 152 also have a slot 160 (Figs. 12 and 13). The slots 160 accommodate bolts 140. The slots 160 are oval-shaped, as shown in Fig. 13, which permits radial adjustment of each anode plate 130 with respect to cathode 110.
  • the anode plates are of titanium or other valve metal.
  • the plates are coated, as mentioned above, on the active anode surface 142 and flanges 136, 138 with a non-passivating coating, for instance a platinum coating.
  • Components of the bracket assembly 150 are similarly manufactured, clad and/or coated.
  • the bolts 140 may be titanium bolts with a fluorocarbon coating to prevent galling, e.g., a Teflon coating.
  • the current distribution bars 152 preferably comprise a copper core having a titanium cladding with a non-passivating coating.
  • Other components immersed in the electrolyte, for instance the cell ribs 116, 118 and adjustment clips 154 are current carrying, and thus are made of titanium with a non-passivating coating such as of platinum at the electrical junctions.
  • busses 180 (Figs. 10 and 11), attached to inner ribs 118.
  • the current flows from the busses 180 through the ribs 116, 118 to each current distribution bar 152, as shown in Fig. 11.
  • the elongated channels 132 (Fig. 10a) are sufficiently flexible that they can be flexed laterally, in the center portion 134 between flanges 136, 138, to the configuration shown in dashed lines in Fig. 10a.
  • the anode plates 132 are initially rolled or otherwise formed so that the center portion 134, thereof, is relatively flat. Flexing the center portion 134 laterally into the concave configuration shown in dashed lines in Fig. 10a is achieved by spreading the flanges 136, 138 apart from each other and slightly truncating them as shown in Fig. 10a.
  • the anode could be rolled or otherwise formed to a convex or concave configuration, and then flexed into a flat configuration by appropriately manipulating the anode flanges 136, 138.
  • the anode flanges 136, 138 are movable both circumferentially and radially in the cell.
  • the anode flanges 136, 138 of the multiple anode plates 130 can be moved simultaneously radially towards the cathode, and at the same time spread apart, increasing the amount of flex or curvature in center portion 134 (Fig. 10a) of each anode plate.
  • the anode flanges 136, 138 of the multiple anode plates 130 can be moved simultaneously away from the cathode, and at the same time brought closer together, to reduce the amount of flex or curvature in the anode plates.
  • the cathode 110 comprises at each end, a circumferential wiper seal 166 (Fig. 11a).
  • the end ribs 116 each support a flanged seal ring 170.
  • Each seal ring 170 extends all of the way around the inside of the cell, in an arc which has an axis coaxial with the cathode 110.
  • Each seal ring 170 extends, as shown in Fig. 11, from the upper edge of one rib 116, on one side of the tank 102, to the upper edge of the rib 116 on the opposite side of the tank 102.
  • the seal rings 170 each have a flange 172 (Fig. 11a).
  • Each flange 172 has an annular slot 174. The slots 174 engage the wiper seals 166 and thereby confine the flow to gap 168.
  • Figs. 10-13 can be employed with a controlled flow apparatus such as disclosed with regard to Figs. 1-9.
  • the anode design of Figs. 1-9 can be employed with a flooded cell design such as disclosed in Figs. 10-13.
  • a seal can be provided between contiguous flanges 136, 138 of adjacent anode plates 130. In this way, the anode plates would define, with the cathode, a completely confined channel through which the electrolyte would flow.
  • the flanges 136, 138 could be undercut to accommodate a seal sealing the assembly against the leakage of electrolyte between the flanges.
  • Fig. 14 shows an alternative embodiment of the present invention in which the anode plates 210 can be flexed into a desired configuration.
  • Each anode plate 210 is provided with a plurality of spaced apart main supports 230 aligned with the center line of the anode plate, a plurality of spaced apart edge aligned supports 240 aligned with one edge 242 of each anode plate, and a plurality of additional edge aligned supports 250, aligned with an opposite edge 252 of each anode plate.
  • Electrolyte is contained in the apparatus within outer rubber-covered shell 260. All of the supports protrude through the shell and are adjustable radially with respect to the shell. The supports are sealed with respect to the shell 260 by seals 262.
  • the cell comprises a plurality of anode plates 310.
  • the anode plates 310 are provided, on their underside, with a plurality of bosses 312 similar to the cell of Figs. 1-9.
  • the bosses protrude into holes 314 of a rubber lined shell 316.
  • the shell 316 is similar to shell 14 of Fig. 1 extending circumferentially around a cathode (not shown).
  • a rubber lining 317 covers the entire inner surface of the shell 316.
  • the bosses are movable radially in the holes 314 and are sealed within the holes by seal rings 318.
  • the bosses 312 are internally bored and threaded. Bolts 320 engage the bosses 312.
  • the bolts 320 are located in holes 314, in a radial direction, by support washers 322 and spacer rings 324. Shims (not shown) similar to support strips 90 (Fig. 8), in shell 316, engage the longitudinally extending parallel opposite edges (not shown) of the anode plates 310. By suitably dimensioning the shims, spacer rings 324, and the amount bolts 320 are turned into bosses 312, the anode plates 310 can be flexed into whatever arcuate configuration is desired.
  • current is supplied to the anode plates by buss connections 326.
  • the spacer rings 324 can function as contact rings, and current can be supplied to the anode plates 310, through the shell 316 and the spacer rings 324.
EP92104923A 1991-03-21 1992-03-20 Elektrolytische Zelle-Anode Expired - Lifetime EP0504939B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US672981 1984-11-19
US67298191A 1991-03-21 1991-03-21

Publications (3)

Publication Number Publication Date
EP0504939A2 true EP0504939A2 (de) 1992-09-23
EP0504939A3 EP0504939A3 (en) 1993-03-17
EP0504939B1 EP0504939B1 (de) 1996-08-28

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP92104923A Expired - Lifetime EP0504939B1 (de) 1991-03-21 1992-03-20 Elektrolytische Zelle-Anode

Country Status (7)

Country Link
EP (1) EP0504939B1 (de)
JP (1) JPH0647758B2 (de)
KR (1) KR100249115B1 (de)
AT (1) ATE141962T1 (de)
CA (1) CA2062089A1 (de)
DE (1) DE69213060T2 (de)
TW (1) TW197534B (de)

Cited By (11)

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FR2720411A1 (fr) * 1994-05-24 1995-12-01 Permelec Electrode Ltd Structure d'électrode à matériau électroconducteur élastique.
WO1997006291A1 (en) * 1995-08-07 1997-02-20 Eltech Systems Corporation Anode electroplating cell
US6051118A (en) * 1994-12-30 2000-04-18 Ishifuku Metal Industry Co., Ltd. Compound electrode for electrolysis
EP1388596A2 (de) * 2002-08-01 2004-02-11 EISENMANN MASCHINENBAU KG (Komplementär: EISENMANN-Stiftung) Anlage zur kataphoretischen Tauchlackierung von Gegenständen
EP1630259A3 (de) * 2004-08-26 2011-06-15 General Electric Company Apparatur zum Elektroplattieren und Methode zur Herstellung einer Anodeneinheit
CN102321895A (zh) * 2011-09-01 2012-01-18 西安航天动力机械厂 一种整体式阳极槽
CN102933752A (zh) * 2010-09-30 2013-02-13 株式会社新克 滚筒用镀敷方法及装置
CN109898102A (zh) * 2017-12-08 2019-06-18 日铁住金工材株式会社 金属箔制造装置以及电极板安装体
CN110565138A (zh) * 2019-09-06 2019-12-13 陕西汉和新材料科技有限公司 一种新型铜箔防氧化槽液下辊机制
CN113529117A (zh) * 2021-05-31 2021-10-22 新乡医学院三全学院 一种电化学反应池
WO2022164695A1 (en) * 2021-02-01 2022-08-04 Lam Research Corporation Spatially and dimensionally non-uniform channelled plate for tailored hydrodynamics during electroplating

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FR2714395B1 (fr) * 1993-12-28 1996-04-05 Lorraine Laminage Anode soluble pour dispositif d'électrodéposition.
WO1998017845A1 (fr) * 1996-10-24 1998-04-30 Ishifuku Metal Industry Co., Ltd. Electrolyseur
JPH11302900A (ja) * 1998-04-17 1999-11-02 Ishifuku Metal Ind Co Ltd 電解装置及びその組立て方法
JP3261582B2 (ja) * 2000-02-04 2002-03-04 株式会社三船鉄工所 電解銅箔の製造装置
US6585846B1 (en) * 2000-11-22 2003-07-01 3M Innovative Properties Company Rotary converting apparatus and method for laminated products and packaging
JP4858666B2 (ja) * 2001-09-27 2012-01-18 Ｔｄｋ株式会社 電極装置
WO2005026412A1 (en) * 2003-09-16 2005-03-24 Global Ionix Inc. An electrolytic cell for removal of material from a solution
JP4038194B2 (ja) * 2004-03-03 2008-01-23 野▲崎▼工業株式会社 不溶性電極及びそれに使用される電極板並びにその使用方法
DE102004025669A1 (de) * 2004-05-21 2005-12-15 Diaccon Gmbh Funktionelle CVD-Diamantschichten auf großflächigen Substraten
JP5414257B2 (ja) * 2008-12-08 2014-02-12 株式会社昭和 電解用電極
JP7005323B2 (ja) * 2017-12-08 2022-01-21 日鉄工材株式会社 金属箔製造装置
KR20230082190A (ko) * 2021-12-01 2023-06-08 에이티엑스 주식회사 동박 제조장치

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US1881713A (en) * 1928-12-03 1932-10-11 Arthur K Laukel Flexible and adjustable anode
US4340449A (en) * 1977-10-11 1982-07-20 Texas Instruments Incorporated Method for selectively electroplating portions of articles
EP0424807A1 (de) * 1989-10-23 1991-05-02 Eltech Systems Corporation Anode einer Elektroplattierungszelle

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CA682872A (en) * 1964-03-24 A. Mcneill John Apparatus for electroplating cylinders
US3170699A (en) * 1963-03-25 1965-02-23 Sperry Rand Corp Manure spreader
US4318794A (en) * 1980-11-17 1982-03-09 Edward Adler Anode for production of electrodeposited foil

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US1881713A (en) * 1928-12-03 1932-10-11 Arthur K Laukel Flexible and adjustable anode
US4340449A (en) * 1977-10-11 1982-07-20 Texas Instruments Incorporated Method for selectively electroplating portions of articles
EP0424807A1 (de) * 1989-10-23 1991-05-02 Eltech Systems Corporation Anode einer Elektroplattierungszelle

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5626730A (en) * 1994-05-24 1997-05-06 Permelec Electrode Ltd. Electrode structure
FR2720411A1 (fr) * 1994-05-24 1995-12-01 Permelec Electrode Ltd Structure d'électrode à matériau électroconducteur élastique.
US6051118A (en) * 1994-12-30 2000-04-18 Ishifuku Metal Industry Co., Ltd. Compound electrode for electrolysis
WO1997006291A1 (en) * 1995-08-07 1997-02-20 Eltech Systems Corporation Anode electroplating cell
US5783058A (en) * 1995-08-07 1998-07-21 Eltech Systems Corporation Anode electroplating cell and method
EP1388596A2 (de) * 2002-08-01 2004-02-11 EISENMANN MASCHINENBAU KG (Komplementär: EISENMANN-Stiftung) Anlage zur kataphoretischen Tauchlackierung von Gegenständen
EP1388596A3 (de) * 2002-08-01 2006-09-27 EISENMANN Maschinenbau GmbH & Co. KG Anlage zur kataphoretischen Tauchlackierung von Gegenständen
EP1630259A3 (de) * 2004-08-26 2011-06-15 General Electric Company Apparatur zum Elektroplattieren und Methode zur Herstellung einer Anodeneinheit
EP2623647A4 (de) * 2010-09-30 2015-09-23 Think Labs Kk Zylinderplattierungsverfahren und -vorrichtung
CN102933752A (zh) * 2010-09-30 2013-02-13 株式会社新克 滚筒用镀敷方法及装置
CN102321895A (zh) * 2011-09-01 2012-01-18 西安航天动力机械厂 一种整体式阳极槽
CN102321895B (zh) * 2011-09-01 2013-10-23 西安航天动力机械厂 一种整体式阳极槽
CN109898102A (zh) * 2017-12-08 2019-06-18 日铁住金工材株式会社 金属箔制造装置以及电极板安装体
CN110565138A (zh) * 2019-09-06 2019-12-13 陕西汉和新材料科技有限公司 一种新型铜箔防氧化槽液下辊机制
WO2022164695A1 (en) * 2021-02-01 2022-08-04 Lam Research Corporation Spatially and dimensionally non-uniform channelled plate for tailored hydrodynamics during electroplating
CN113529117A (zh) * 2021-05-31 2021-10-22 新乡医学院三全学院 一种电化学反应池

Also Published As

Publication number Publication date
KR920018247A (ko) 1992-10-21
ATE141962T1 (de) 1996-09-15
JPH0647758B2 (ja) 1994-06-22
JPH04346697A (ja) 1992-12-02
DE69213060D1 (de) 1996-10-02
EP0504939A3 (en) 1993-03-17
KR100249115B1 (ko) 2000-04-01
TW197534B (de) 1993-01-01
EP0504939B1 (de) 1996-08-28
DE69213060T2 (de) 1997-01-23
CA2062089A1 (en) 1992-09-22

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