EP0430917B1 - Device for the electrolytic deposition of a continuous layer with a constant thickness - Google Patents
Device for the electrolytic deposition of a continuous layer with a constant thickness Download PDFInfo
- Publication number
- EP0430917B1 EP0430917B1 EP90870223A EP90870223A EP0430917B1 EP 0430917 B1 EP0430917 B1 EP 0430917B1 EP 90870223 A EP90870223 A EP 90870223A EP 90870223 A EP90870223 A EP 90870223A EP 0430917 B1 EP0430917 B1 EP 0430917B1
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- European Patent Office
- Prior art keywords
- cathode
- anode
- modules
- anodic
- module
- Prior art date
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- Expired - Lifetime
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- 230000008021 deposition Effects 0.000 title description 7
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 28
- 239000003792 electrolyte Substances 0.000 claims abstract description 26
- 239000000758 substrate Substances 0.000 claims abstract description 20
- 239000000463 material Substances 0.000 claims description 7
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 4
- 239000004810 polytetrafluoroethylene Substances 0.000 description 4
- 239000004698 Polyethylene Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- -1 polytetrafluoroethylene Polymers 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 2
- 229910010293 ceramic material Inorganic materials 0.000 description 2
- 238000005137 deposition process Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 229940082150 encore Drugs 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910000856 hastalloy Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 210000000056 organ Anatomy 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000011253 protective coating Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
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- 239000010936 titanium Substances 0.000 description 1
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Images
Classifications
-
- 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
- C25D7/00—Electroplating characterised by the article coated
- C25D7/06—Wires; Strips; Foils
- C25D7/0607—Wires
Definitions
- the present invention relates to a device for forming a continuous electrolytic deposit of constant thickness on a mobile substrate, such as a moving metal strip. It more particularly aims at achieving a small and regular distance between the anode and the cathode, so as to allow the use of high current densities while limiting the ohmic losses in the electrolyte.
- the device of the invention applies both to the deposition of a permanent protective coating on a metal strip and to the manufacture of a thin sheet, then separated from the substrate on which it has been formed.
- a permanent protective coating on a metal strip
- a thin sheet then separated from the substrate on which it has been formed.
- an electrolytic deposition device comprising a circular cathode and an anode constituted by a plurality of anode modules.
- the cathode formed by the substrate passes in front of these anodes with a spacing which can vary as a function of deformations, mechanical or thermal, of the substrate itself or of its support and guide rollers.
- the geometric shape of the substrate and / or of its support and guide rollers may also have imperfections which have an adverse effect on the regularity of the electrolysis interval.
- this electrolysis interval is as regular as possible, that is to say that its variations are kept within as narrow limits as possible. Indeed, these variations acquire a relative importance all the greater as the electrolysis interval is narrower, and this results in corresponding variations in the resistance of the electrical circuit, the current density and finally the efficiency. of the electrolytic deposition process.
- the object of the present invention is to propose a device making it possible to remedy this drawback by ensuring the regularity of the electrolysis interval by simple means, even in the event of deformation of the substrate and / or of its support and guide rollers. .
- a device for forming a continuous electrolytic deposit of constant thickness on a mobile substrate in which a cathode, constituted by said mobile substrate, passes in front of an anode with which it delimits an electrolysis interval of low height , said anode consisting of a plurality of anode modules and having orifices which open into said electrolysis interval, is characterized in that said anode modules are mechanically independent of each other, in that the electric circuits , respectively hydraulic supplying said anode modules have flexible sections between the fixed current sources, respectively electrolyte, and said anode modules, in that said anode modules are provided with means by which they bear on the cathode or on a surface directly connected to the cathode.
- said support means of at least one anode module comprise means for adjusting the distance between said anode module and the cathode or the surface directly linked to the cahtode.
- a surface directly linked to the cathode is a bearing surface which is at a known distance, preferably constant, from the cathode.
- these are, for example, the surface of the drum of a radial electrolysis cell, against which the substrate is applied during its passage through the electrolytic solution; in this case, the distance between the cathode and the surface directly linked to the cathode is equal to the thickness of the product to be coated at any point in the electrolysis interval.
- this surface directly linked to the cathode can be materialized in particular by cathode support rollers along its rectilinear trajectory.
- the support members are for example constituted by pads with a low coefficient of friction, or by rollers, which slide, respectively which roll on the cathode or on the surface directly linked to the cathode.
- the device of the invention comprises an electrolysis cell delimited by an enclosure surrounding at least one anode module
- said adjustable support means are, at least in part, located inside the electrolysis cell.
- at least said part is made of a material resistant to the electrolyte.
- said electrolyte resistant material is preferably electrically insulating, or the members which it constitutes are electrically isolated from the anode and / or the cathode, in order to avoid an anodic attack on these members or on the contrary. a cathodic deposit on these same organs.
- said adjustable support means are located outside the electrolysis cell.
- said support means comprise hollow arms, which provide both mechanical support and hydraulic supply anode modules.
- the anode modules are preferably provided with an individual hydraulic supply, for example from a large section manifold located outside the electrolysis cell.
- Fig. 1 illustrates the principle of the device of the invention in the case of a radial electrolysis cell of the conventional type.
- the electrolysis cell comprises a cathode, constituted by a roller 1 for deflecting the substrate 2, and an anode arranged opposite at least part of the periphery of the roller 1, at a predetermined distance from that -this.
- the anode consists of a plurality of anode modules 3, mechanically independent of one another, which are each provided with support means 4 on the cathode roller 1 or on the substrate 2.
- the arrow a indicates the direction of rotation of the roller 1; the arrows b symbolize the mechanical independence of the anode modules 3.
- the roller cathode 1 and the anode namely here the anode modules 3, are generally immersed in the electrolyte bath.
- the anode modules 3 can be constituted by particular anodes of the type described in the aforementioned patents BE-A-905,588 and BE-A-08,700,561.
- FIG. 2 shows an example of mounting an anode module 3 provided with support means situated inside the electrolysis cell, seen in direction A of FIG. 1.
- the anode modules 3 and their support means 4 are immersed in the electrolyte, symbolized by the hatched area 5.
- the metal parts of the cathode and anode modules are of preferably made of titanium or an alloy such as hastelloy or of stainless steel; the support means comprise for example pads 4 in P T F E, which have a low coefficient of friction, while also being insensitive to the electrolyte.
- the pads 4 are here arranged on either side of the deposition zone 6 corresponding to the substrate 2.
- the pads 4 can be provided with adjustment means, known per se and not shown here, to vary the distance between the substrate 2 and the anode module 3 and / or to correct the variations in this distance due for example to the wear of the pads 4.
- these adjustment means can be constituted by vertical threaded rods provided with nuts for adjusting the position of the anode module.
- Figs. 3 to 5 illustrate various examples of mounting an anode module 3, the support means 4 of which are located outside the electrolysis cell.
- the anode module 3 is surrounded by an enclosure 7 which contains the electrolyte 5; this enclosure 7 extends axially over a width at least equal to the width of the deposition zone 6 or of the substrate 2, and on the periphery over at least part of the periphery of the roller 1, to which it is connected by seals rotary seals 8.
- seals 8 thus ensure sealing between the active part and the parts for supporting the cathode roller 1.
- the substrate 2 and the deposition zone 6 are similar to those of FIG. 1.
- the entire anode module 3 is seen in the direction A of FIG. 1.
- the circulation of the electrolyte is ensured by means known per se, in particular by the two aforementioned Belgian patents, which are not part of the present invention and which are therefore not shown.
- the anode module 3 is provided with two bent arms 9, 10 which pass respectively through the side walls of the enclosure 7 and bear, by their outer end, on the surface of the roller 1.
- These arms 9, 10 are provided, at their outer end, support means constituted for example by rollers 4, which roll on the roller 1.
- rollers are preferably made of a wear-resistant material, such as a ceramic material or a synthetic material such as PTFE, polyethylene (PE) or polypropylene (PP).
- PTFE polyethylene
- PP polypropylene
- the tightness of the bushings 11, 12 of the walls of the enclosure 7 by the arms 9, 10 is ensured by any means known per se, for example by flexible membranes or bellows made of a material resistant to the electrolyte such as rubber. , PTFE, PE or P P.
- FIG. 4 is substantially identical to that of FIG. 3.
- the essential difference is that the rotary seals 8 are transferred to the bottom of grooves made in the roller 1. This results in a reduction in the peripheral length of the seals 8, which reduces the risk of electrolyte leakage. ; in addition, the bearing areas of the roller 1 are thus clearly separated from the active area exposed to the electrolyte 5.
- FIG. 5 Another possible arrangement is illustrated in FIG. 5.
- the two arms 9 and 10 are joined together in a stirrup spanning the enclosure 7 and resting on the roller 1 by support means such as rollers 4.
- This stirrup 9, 10 is provided with a central branch 13 which enters the enclosure 7 through a passage 14 pierced in the rear wall of the enclosure 7, and which carries the anode module 3.
- the sealing of the crossing 14 is also ensured by known means per se such as a flexible membrane or a bellows made of a material resistant to the electrolyte 5.
- Fig. 6 illustrates a particular arrangement making it possible to supply each anode module with electrolyte individually, the support means of which are located outside the electrolysis cell.
- the arm 10 consists of a tube which is connected to a supply manifold 16 by means of a flexible element such as a bellows 15.
- the enclosure 7 acts as an outlet manifold , from which the electrolyte 5 is withdrawn by known means, not shown, and optionally returned to the supply collector after an appropriate treatment.
- the other numerical marks correspond to the identical marks of FIGS. 3 to 5.
- This arrangement simplifies the mounting of the anode modules, eliminating at least part of the conventional external hydraulic circuits.
Abstract
Description
La présente invention concerne un dispositif pour former un dépôt électrolytique continu d'épaisseur constante sur un substrat mobile, tel qu'une bande métallique en défilement. Elle vise plus particulièrement la réalisation d'une distance faible et régulière entre l'anode et la cathode, de façon, à permettre l'emploi de densités de courant élevées tout en limitant les pertes ohmiques dans l'électrolyte.The present invention relates to a device for forming a continuous electrolytic deposit of constant thickness on a mobile substrate, such as a moving metal strip. It more particularly aims at achieving a small and regular distance between the anode and the cathode, so as to allow the use of high current densities while limiting the ohmic losses in the electrolyte.
Le dispositif de l'invention s'applique aussi bien au dépôt d'un revêtement protecteur permanent sur une bande de métal qu'à la fabrication d'une feuille mince, séparée ensuite du substrat sur lequel elle a été formée. Dans la description qui va suivre, on se réfèrera pour simplifier à un dépôt ou à un revêtement électrolytique.The device of the invention applies both to the deposition of a permanent protective coating on a metal strip and to the manufacture of a thin sheet, then separated from the substrate on which it has been formed. In the description which follows, reference will be made for simplicity to an electrolytic deposit or coating.
On sait que l'utilisation d'un intervalle d'électrolyse étroit, c'est-à-dire d'une faible distance entre l'anode et la cathode, permet de réaliser des vitesses élevées de circulation de l'électrolyte dans cet intervalle sans nécessiter des débits globaux trop élevés. Il est possible, dans ces conditions, d'appliquer des densités de courant élevées, qui conduisent à de hauts rendements de dépôt électrolytique.It is known that the use of a narrow electrolysis interval, that is to say a short distance between the anode and the cathode, makes it possible to achieve high speeds of circulation of the electrolyte in this interval without requiring too high overall flow rates. It is possible, under these conditions, to apply high current densities, which lead to high yields of electrolytic deposition.
Par ailleurs, il est également connu qu'un intervalle d'électrolyse étroit permet de réduire les pertes électriques causées par la résistivité de l'électrolyte.Furthermore, it is also known that a narrow electrolysis interval makes it possible to reduce the electrical losses caused by the resistivity of the electrolyte.
On connaît, notamment par les brevets BE-A-905588 et BE-A-08700561, des anodes assurant un court chemin de l'électrolyte dans un intervalle d'électrolyse étroit, avec une forte turbulence et un faible débit, et permettant dès lors d'utiliser des densités de courant élevées.Known, in particular by patents BE-A-905588 and BE-A-08700561, anodes ensuring a short path of the electrolyte in a narrow electrolysis interval, with high turbulence and a low flow rate, and therefore allowing to use high current densities.
On connaît également, par le brevet US-A-2271735, un dispositif de dépôt électrolytique comportant une cathode circulaire et une anode constituée par une pluralité de modules anodiques.Also known, from US-A-2271735, an electrolytic deposition device comprising a circular cathode and an anode constituted by a plurality of anode modules.
Il subsiste néanmoins avec les anodes connues, un problème concernant la régularité de l'intervalle d'électrolyse. En effet, la cathode constituée par le substrat défile devant ces anodes avec un écartement qui peut varier en fonction de déformations, mécaniques ou thermiques, du substrat lui-même ou de ses rouleaux de soutien et de guidage. En outre, la forme géométrique du substrat et/ou de ses rouleaux de soutien et de guidage peut également présenter des imperfections qui se répercutent défavorablement sur la régularité de l'intervalle d'électrolyse.However, with the known anodes, there remains a problem concerning the regularity of the electrolysis interval. In fact, the cathode formed by the substrate passes in front of these anodes with a spacing which can vary as a function of deformations, mechanical or thermal, of the substrate itself or of its support and guide rollers. In addition, the geometric shape of the substrate and / or of its support and guide rollers may also have imperfections which have an adverse effect on the regularity of the electrolysis interval.
Il est cependant essentiel que cet intervalle d'électrolyse soit aussi régulier que possible, c'est-à-dire que ses variations soient maintenues dans des limites aussi étroites que possible. En effet, ces variations acquièrent une importance relative d'autant plus grande que l'intervalle d'électrolyse est plus étroit, et il en résulte des variations correspondantes de la résistance du circuit électrique, de la densité de courant et finalement de l'efficacité du processus de dépôt électrolytique.It is however essential that this electrolysis interval is as regular as possible, that is to say that its variations are kept within as narrow limits as possible. Indeed, these variations acquire a relative importance all the greater as the electrolysis interval is narrower, and this results in corresponding variations in the resistance of the electrical circuit, the current density and finally the efficiency. of the electrolytic deposition process.
La présente invention a pour objectif de proposer un dispositif permettant de remédier à cet inconvénient en assurant la régularité de l'intervalle d'électrolyse par des moyens simples, même en cas de déformation du substrat et/ou de ses rouleaux de soutien et de guidage.The object of the present invention is to propose a device making it possible to remedy this drawback by ensuring the regularity of the electrolysis interval by simple means, even in the event of deformation of the substrate and / or of its support and guide rollers. .
Conformément à la présente invention, un dispositif pour former un dépôt électrolytique continu d'épaisseur constante sur un substrat mobile, dans lequel une cathode, constituée par ledit substrat mobile, défile devant une anode avec laquelle elle délimite un intervalle d'électrolyse de faible hauteur, ladite anode étant constituée d'une pluralité de modules anodiques et présentant des orifices qui débouchent dans ledit intervalle d'électrolyse, est caractérisé en ce que lesdits modules anodiques sont mécaniquement indépendants l'un de l'autre, en ce que les circuits électrique, respectivement hydrauliques alimentant lesdits modules anodiques comportent des tronçons flexibles entre les sources fixes de courant, respectivement d'électrolyte, et lesdits modules anodiques, en ce que lesdits modules anodiques sont pourvus de moyens par lesquels ils prennent appui sur la cathode ou sur une surface directement liée à la cathode.According to the present invention, a device for forming a continuous electrolytic deposit of constant thickness on a mobile substrate, in which a cathode, constituted by said mobile substrate, passes in front of an anode with which it delimits an electrolysis interval of low height , said anode consisting of a plurality of anode modules and having orifices which open into said electrolysis interval, is characterized in that said anode modules are mechanically independent of each other, in that the electric circuits , respectively hydraulic supplying said anode modules have flexible sections between the fixed current sources, respectively electrolyte, and said anode modules, in that said anode modules are provided with means by which they bear on the cathode or on a surface directly connected to the cathode.
Il s'est d'ailleurs avéré intéressant, dans le cadre de l'invention, que lesdits moyens d'appui d'au moins un module anodique comportent des moyens de réglage de la distance entre ledit module anodique et la cathode ou la surface directement liée à la cahtode.It has also been found advantageous, within the framework of the invention, that said support means of at least one anode module comprise means for adjusting the distance between said anode module and the cathode or the surface directly linked to the cahtode.
Au sens de la présente demande, une surface directement liée à la cathode est une surface d'appui qui se trouve à une distance connue, de préférence constante, de la cathode. Il s'agit par exemple, de la surface du tambour d'une cellule d'électrolyse radiale, contre laquelle le substrat est appliqué pendant son passage dans la solution électrolytique; dans ce cas, la distance entre la cathode et la surface directement liée à la cathode est égale à l'épaisseur du produit à revêtir en tout point de l'intervalle d'électrolyse. Dans une cellule droite, où le substrat cathodique suit une trajectoire rectiligne devant l'anode, cette surface directement liée à la cathode peut être matérialisée notamment par des rouleaux de support de la cathode le long de sa trajectoire rectiligne.Within the meaning of the present application, a surface directly linked to the cathode is a bearing surface which is at a known distance, preferably constant, from the cathode. These are, for example, the surface of the drum of a radial electrolysis cell, against which the substrate is applied during its passage through the electrolytic solution; in this case, the distance between the cathode and the surface directly linked to the cathode is equal to the thickness of the product to be coated at any point in the electrolysis interval. In a straight cell, where the cathode substrate follows a rectilinear trajectory in front of the anode, this surface directly linked to the cathode can be materialized in particular by cathode support rollers along its rectilinear trajectory.
Les organes d'appui sont par exemple constitués par des patins à faible coefficient de frottement, ou par des galets, qui glissent, respectivement qui roulent sur la cathode ou sur la surface directement liée à la cathode.The support members are for example constituted by pads with a low coefficient of friction, or by rollers, which slide, respectively which roll on the cathode or on the surface directly linked to the cathode.
Suivant une mise en oeuvre particulière, le dispositif de l'invention comporte une cellule d'électrolyse délimitée par une enceinte entourant au moins un module anodiqueAccording to a particular implementation, the device of the invention comprises an electrolysis cell delimited by an enclosure surrounding at least one anode module
Selon une réalisation particulière du dispositif de l'invention, lesdits moyens d'appui réglables sont, au moins en partie, situés à l'intérieur de la cellule d'électrolyse. Dans ce cas, au moins ladite partie est réalisée en un matériau résistant à l'électrolyte. A titre d'exemple, les parties sont réalisées en P T F E (= polytétrafluoréthylène), tandis que les galets sont constitués d'un matériau céramique ou d'acier inoxydable.According to a particular embodiment of the device of the invention, said adjustable support means are, at least in part, located inside the electrolysis cell. In this case, at least said part is made of a material resistant to the electrolyte. For example, the parts are made of PTFE (= polytetrafluoroethylene), while the rollers are made of a ceramic material or stainless steel.
En outre, ledit matériau résistant à l'électrolyte est de préférence électriquement isolant, ou les organes qu'il constitue sont électriquement isolés de l'anode et/ou de la cathode, afin d'éviter une attaque anodique de ces organes ou au contraire un dépôt cathodique sur ces mêmes organes.In addition, said electrolyte resistant material is preferably electrically insulating, or the members which it constitutes are electrically isolated from the anode and / or the cathode, in order to avoid an anodic attack on these members or on the contrary. a cathodic deposit on these same organs.
Suivant une autre réalisation du dispositif de l'invention, lesdits moyens d'appui réglables sont situés à l'extérieur de la cellule d'électrolyse.According to another embodiment of the device of the invention, said adjustable support means are located outside the electrolysis cell.
Cette disposition laisse plus de liberté pour le choix des matériaux utilisables et offre de plus grandes facilités de réglage; elle requiert cependant que l'on assure une étanchéité suffisante entre l'intérieur et l'extérieur de la cellule, notamment le long des pièces mécaniques qui relient les modules anodiques à leurs appuis, entre la portion active et la portion d'appui de la cathode, et éventuellement le long des arrivées de courant électrique aux modules anodiques.This arrangement leaves more freedom for the choice of usable materials and offers greater ease of adjustment; however, it requires sufficient sealing between the inside and outside of the cell, in particular along the mechanical parts which connect the anode modules to their supports, between the active portion and the support portion of the cathode, and possibly along the electrical current inlets to the anode modules.
Selon une mise en oeuvre particulière du dispositif avec des moyens d'appui réglables situés à l'extérieur de la cellule d'électrolyse, lesdits moyens d'appui comportent des bras creux, qui assurent à la fois le support mécanique et l'alimentation hydraulique des modules anodiques. Dans ce cas, les modules anodiques sont de préférence dotés d'une alimentation hydraulique individuelle, par exemple à partir d'un collecteur de grande section situé à l'extérieur de la cellule d'électrolyse.According to a particular implementation of the device with adjustable support means situated outside the electrolysis cell, said support means comprise hollow arms, which provide both mechanical support and hydraulic supply anode modules. In this case, the anode modules are preferably provided with an individual hydraulic supply, for example from a large section manifold located outside the electrolysis cell.
La description détaillée qui va suivre permettra de dégager d'autres caractéristiques et avantages du dispositif de l'invention. Cette description porte sur un certain nombre de réalisations particulières de ce dispositif qui sont illustrées dans les dessins annexés dans lesquels la
- Fig. 1
- présente le principe du dispositif de l'invention, appliqué à une cellule d'électrolyse radiale; la
- Fig. 2
- montre un exemple de montage d'un module anodique pourvu de moyens d'appui situés à l'intérieur de la cellule; la
- Fig. 3
- montre un exemple de montage d'un module anodique pourvu de moyens d'appui situés à l'extérieur de la cellule; la
- Fig. 4
- montre un autre exemple de montage d'un module anodique pourvu de moyens d'appui situés à l'extérieur de la cellule; la
- Fig. 5
- montre encore un autre exemple de montage d'un module anodique pourvu de moyens d'appui situés à l'extérieur de la cellule; la
- Fig. 6
- présente un mode de réalisation dans lequel les bras des moyens d'appui extérieurs constituent des éléments du circuit hydraulique.
- Fig. 1
- presents the principle of the device of the invention, applied to a radial electrolysis cell; the
- Fig. 2
- shows an example of mounting an anode module provided with support means located inside the cell; the
- Fig. 3
- shows an example of mounting an anode module provided with support means located outside the cell; the
- Fig. 4
- shows another example of mounting an anode module provided with support means located outside the cell; the
- Fig. 5
- shows yet another example of mounting an anode module provided with support means located outside the cell; the
- Fig. 6
- presents an embodiment in which the arms of the external support means constitute elements of the hydraulic circuit.
Ces figures constituent des représentations schématiques, sans échelle particulière, dans lesquelles on n'a reproduit que les éléments directement nécessaires à la compréhension de l'invention. Les sens de circulation des fluides, tant électrique qu'hydraulique, est indiqué par des flèches appropriées. Des éléments identiques ou analogues, ou assurant des fonctions identiques ou analogues, sont désignés par les mêmes repères numériques dans toutes les figures.These figures constitute schematic representations, without any particular scale, in which only the elements directly necessary for understanding the invention have been reproduced. The directions of fluid flow, both electrical and hydraulic, are indicated by appropriate arrows. Identical or analogous elements, or ensuring identical or analogous functions, are designated by the same reference numerals in all the figures.
La Fig. 1 illustre le principe du dispositif de l'invention dans le cas d'une cellule d'électrolyse radiale de type conventionnel.Fig. 1 illustrates the principle of the device of the invention in the case of a radial electrolysis cell of the conventional type.
De façon connue en soi, la cellule d'électrolyse comporte une cathode, constituée par un rouleau 1 de déviation du substrat 2, et une anode disposée en face d'au moins une partie du pourtour du rouleau 1, à une distance prédéterminée de celui-ci.In a manner known per se, the electrolysis cell comprises a cathode, constituted by a
Suivant la présente invention, l'anode se compose d'une pluralité de modules anodiques 3, mécaniquement indépendants l'un de l'autre, qui sont chacun pourvus de moyens d'appui 4 sur le rouleau cathodique 1 ou sur le substrat 2. La flèche a indique le sens de rotation du rouleau 1; les flèches b symbolisent l'indépendance mécanique des modules anodiques 3.According to the present invention, the anode consists of a plurality of
On rappellera enfin que, dans une cellule de ce type, le rouleau cathodique 1 et l'anode, à savoir ici les modules anodiques 3, sont généralement immergés dans le bain d'électrolyte. Dans le cadre de la présente invention, les modules anodiques 3 peuvent être constitués par des anodes particulières du type décrit dans les brevets BE-A-905588 et BE-A-08700561 précités.Finally, it will be recalled that, in a cell of this type, the
La figure 2 montre un exemple de montage d'un module anodique 3 pourvu de moyens d'appui situés à l'intérieur de la cellule d'électrolyse, vu suivant la direction A de la Fig. 1. Dans cette disposition, les modules anodiques 3 et leurs moyens d'appui 4 sont immergés dans l'électrolyte, symbolisé par la zone hachurée 5. Pour résister à l'électrolyte, les parties métalliques de la cathode et des modules anodiques sont de préférence réalisées en titane ou en un alliage tel que le hastelloy ou en un acier inoxydable; les moyens d'appui comprennent par exemple des patins 4 en P T F E, qui présentent un faible coefficient de frottement, tout en étant également insensibles à l'électrolyte.FIG. 2 shows an example of mounting an
Comme on le voit dans la Fig. 2, les patins 4 sont ici disposés de part et d'autre de la zone de dépôt 6 correspondant au substrat 2. Les patins 4 peuvent être pourvus de moyens de réglage, connus en soi et non représentés ici, pour faire varier la distance entre le substrat 2 et le module anodique 3 et/ou pour corriger les variations de cette distance dues par exemple à l'usure des patins 4. A titre d'exemple, ces moyens de réglage peuvent être constitués par des tiges filetées verticales pourvues d'écrous de réglage de la position du module anodique.As seen in Fig. 2, the
Les Fig. 3 à 5 illustrent divers exemples de montage d'un module anodique 3 dont les moyens d'appui 4 sont situés à l'extérieur de la cellule d'électrolyse. Dans cette disposition, le module anodique 3 est entouré par une enceinte 7 qui contient l'électrolyte 5; cette enceinte 7 s'étend axialement sur une largeur au moins égale à la largeur de la zone de dépôt 6 ou du substrat 2, et en périphérie sur au moins une partie du pourtour du rouleau 1, auquel elle se raccorde par des joints d'étanchéité tournants 8. Ces joints 8 assurent ainsi l'étanchéité entre la partie active et les parties d'appui du rouleau cathodique 1. Le substrat 2 et la zone de dépôt 6 sont analogues à ceux de la Fig. 1. Ici également, l'ensemble du module anodique 3 est vu suivant la direction A de la Fig. 1. La circulation de l'électrolyte est assurée par des moyens connus en soi, notamment par les deux brevets belges précités, qui ne font pas partie de la présente invention et qui ne sont dès lors pas représentés.Figs. 3 to 5 illustrate various examples of mounting an
Dans la Fig. 3, le module anodique 3 est pourvu de deux bras coudés 9, 10 qui traversent respectivement les parois latérales de l'enceinte 7 et prennent appui, par leur extrémité extérieure, sur la surface du rouleau 1. Ces bras 9, 10 sont pourvus, à leur extrémité extérieure, de moyens d'appui constitués par exemple par des galets 4, qui roulent sur le rouleau 1. Ces galets sont de préférence réalisés en un matériau résistant à l'usure, tel qu'un matériau céramique ou un matériau synthétique comme le P T F E, le polyéthylène (P E) ou le polypropylène (P P). L'étanchéité des traversées 11, 12 des parois de l'enceinte 7 par les bras 9, 10 est assurée par tout moyen connu en soi, par exemple par des membranes souples ou des soufflets en un matériau résistant à l'électrolyte comme le caoutchouc, le P T F E, le P E ou le P P.In Fig. 3, the
La disposition de la Fig. 4 est sensiblement identique à celle de la Fig. 3. La différence essentielle est que les joints d'étanchéité tournants 8 sont reportés au fond de gorges ménagées dans le rouleau 1. Il en résulte une diminution de la longueur périphérique des joints 8, ce qui réduit les risques de fuite de l'électrolyte; en outre, les zones d'appui du rouleau 1 sont ainsi nettement séparées de la zone active exposée à l'électrolyte 5.The arrangement of FIG. 4 is substantially identical to that of FIG. 3. The essential difference is that the rotary seals 8 are transferred to the bottom of grooves made in the
Une autre disposition possible est illustrée dans la Fig. 5. Ici, les deux bras 9 et 10 sont réunis en un étrier enjambant l'enceinte 7 et reposant sur le rouleau 1 par des moyens d'appui tels que des galets 4. Cet étrier 9, 10 est pourvu d'une branche centrale 13 qui pénètre dans l'enceinte 7 par une traversée 14 percée dans la paroi arrière de l'enceinte 7, et qui porte le module anodique 3. L'étanchéité de la traversée 14 est également assurée par un moyen connu en soi tel qu'une membrane souple ou un soufflet en un matériau résistant à l'électrolyte 5.Another possible arrangement is illustrated in FIG. 5. Here, the two
Dans les cas, illustrés notamment par les Fig. 3 à 5, où les moyens d'appui des modules anodiques sont situés à l'extérieur de la cellule d'électrolyse, c'est-à-dire en fait à l'extérieur de l'enceinte 7, l'arrivée et le retour de l'électrolyte à l'enceinte 7 et aux modules anodiques 3 peuvent être effectués par un circuit hydraulique conventionnel. Il s'est cependant avéré intéressant d'alimenter individuellement chaque module anodique en électrolyte, afin d'assurer une plus grande souplesse dans la conduite et le réglage du processus de dépôt électrolytique.In the cases, illustrated in particular by FIGS. 3 to 5, where the support means of the anode modules are located outside the electrolysis cell, that is to say in fact outside the
La Fig. 6 illustre une disposition particulière permettant d'alimenter individuellement en électrolyte chaque module anodique dont les moyens d'appui sont situés à l'extérieur de la cellule d'électrolyse.Fig. 6 illustrates a particular arrangement making it possible to supply each anode module with electrolyte individually, the support means of which are located outside the electrolysis cell.
Dans cette disposition, le bras 10 est constitué d'un tube qui est raccordé à un collecteur d'alimentation 16 par l'intermédiaire d'un élément souple tel qu'un soufflet 15. L'enceinte 7 joue le rôle de collecteur de sortie, d'où l'électrolyte 5 est soutiré par des moyens connus, non représentés, et éventuellement renvoyé au collecteur d'alimentation après un traitement approprié. Les autres repères numériques correspondent aux repères identiques des Fig. 3 à 5.In this arrangement, the
Cette disposition permet de simplifier le montage des modules anodiques, en supprimant au moins une partie des circuits hydrauliques extérieurs conventionnels.This arrangement simplifies the mounting of the anode modules, eliminating at least part of the conventional external hydraulic circuits.
Il ne sortirait d'ailleurs pas du cadre de la présente invention d'assurer également la sortie de l'électrolyte au moyen d'un bras 9 tubulaire raccordé à un collecteur de sortie analogue au collecteur d'alimentation 16.It would moreover not go beyond the scope of the present invention to also ensure the exit of the electrolyte by means of a
Il faut comprendre que l'invention n'est pas limitée aux modes de réalisation particuliers qui viennent d'être décrits et illustrés. De nombreuses modifications peuvent être envisagées, notamment dans la forme et la disposition des moyens d'appui des modules anodiques ainsi que dans la disposition des modules anodiques, en particulier pour leur utilisation, mutatis mutandis, avec une cellule d'électrolyse rectiligne.It should be understood that the invention is not limited to the modes of particular realization which have just been described and illustrated. Many modifications can be envisaged, in particular in the shape and arrangement of the support means of the anode modules as well as in the arrangement of the anode modules, in particular for their use, mutatis mutandis, with a rectilinear electrolysis cell.
Claims (8)
- Device for forming a continuous electrolytic deposit of a constant thickness on a movable substrate, device wherein a cathode, which is constituted by the said movable substrate, is moving forward in front of an anode with which it delimits an electrolysis gap of a small height, the said anode being constituted by a plurality of anodic modules and showing orifices which are opening into the said electrolysis gap, characterized in that the said anodic modules (3) are mechanically independent of each other, in that the electric circuits, respectively the hydraulic circuits, which are feeding the said anodic modules (3), comprise flexible sections (15) between the fixed sources of current, respectively of electrolyte, and the said anodic modules, and in that the said anodic modules are provided with means (4, 9, 10) by which they are supported on the cathode (2) or on a surface (1) directly linked to the cathode.
- Device according to the claim 1, characterized in that the said support means (4) of at least one anodic module (3) comprise means for adjusting the distance between the said anodic module (3) and the cathode (2) or the surface (1) directly linked to the cathode.
- Device according to any of the claims 1 and 2, characterized in that it comprises an electrolytic cell which is delimited by an enclosure (7) surrounding at least one anodic module (3).
- Device according to the claim 3, characterized in that the said support means (4) of the anodic modules (3) are located inside the electrolytic cell.
- Device according to the claim 4, characterized in that the said support means of the anodic modules (3) comprise shoes made of a material presenting a low coefficient of friction.
- Device according to the claim 3, characterized in that the said support means (4) of the anodic modules (3) are located outside the electrolytic cell.
- Device according to the claim 6, characterized in that the said support means comprise arms (9, 10, 13) which pass through the walls of the said enclosure (7) and take are supported on the cathode (2) or on a surface (1) directly linked to the cathode.
- Device according to the claim 7, characterized in that at least one of the arms (9, 10) is constituted by a tube and is used for feeding the electrolyte to, respectively for draining off the electrolyte from the corresponding anodic module (3).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BE8901269A BE1003438A6 (en) | 1989-11-27 | 1989-11-27 | DEVICE FOR FORMING A CONTINUOUS ELECTROLYTIC DEPOSIT OF CONSTANT THICKNESS. |
BE8901269 | 1989-11-27 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0430917A1 EP0430917A1 (en) | 1991-06-05 |
EP0430917B1 true EP0430917B1 (en) | 1995-08-16 |
Family
ID=3884409
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP90870223A Expired - Lifetime EP0430917B1 (en) | 1989-11-27 | 1990-11-21 | Device for the electrolytic deposition of a continuous layer with a constant thickness |
Country Status (6)
Country | Link |
---|---|
US (1) | US5124015A (en) |
EP (1) | EP0430917B1 (en) |
JP (1) | JPH03180485A (en) |
AT (1) | ATE126554T1 (en) |
BE (1) | BE1003438A6 (en) |
DE (1) | DE69021697D1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100429154B1 (en) * | 2001-06-15 | 2004-04-28 | 주식회사 포스코 | Anode bridge and an apparatus for controlling the gag between conductor roll and anode |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2271735A (en) * | 1938-07-16 | 1942-02-03 | Hanson Van Winkle Munning Co | Machine for electroprocessing metal strip |
FR2262369A1 (en) * | 1974-02-25 | 1975-09-19 | Mishima Kosan Co Ltd | Magnetic tape prodn by electrolytic deposn - on a carrier passing through several independent cells |
FR2271306A1 (en) * | 1974-05-13 | 1975-12-12 | Moshima Kosan Co Ltd | Mfg. thin metal films by electrodeposition - such as a nickel-iron-molybdenum alloy with anisotropic magnetic properties |
JPS63140100A (en) * | 1986-12-02 | 1988-06-11 | Kawasaki Steel Corp | Electrolytic treatment cell |
-
1989
- 1989-11-27 BE BE8901269A patent/BE1003438A6/en not_active IP Right Cessation
-
1990
- 1990-11-21 DE DE69021697T patent/DE69021697D1/en not_active Expired - Lifetime
- 1990-11-21 EP EP90870223A patent/EP0430917B1/en not_active Expired - Lifetime
- 1990-11-21 AT AT90870223T patent/ATE126554T1/en not_active IP Right Cessation
- 1990-11-26 JP JP2325123A patent/JPH03180485A/en active Pending
- 1990-11-27 US US07/618,568 patent/US5124015A/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
US5124015A (en) | 1992-06-23 |
DE69021697D1 (en) | 1995-09-21 |
ATE126554T1 (en) | 1995-09-15 |
JPH03180485A (en) | 1991-08-06 |
EP0430917A1 (en) | 1991-06-05 |
BE1003438A6 (en) | 1992-03-24 |
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