WARLIMONT HANS (DE)
| GB2243618A | 1991-11-06 | |||
| DE585633C | 1933-10-12 | |||
| EP0490061A2 | 1992-06-17 |
| 1. | A continuous electroforming process to form a strip for battery electrodes, comprising the steps of: providing a mandrel (1) having on its surface a reusable pattern subdivided into conductive and nonconductive areas ; moving said mandrel (1) through an electroforming bath (2) to deposit a metal layer on said mandrel (1) while it moves through the electroforming bath until the metal layer has assumed the shape of the conductive pattern and a thickness at least sufficient to provide strength for the layer to be removed in strip form (5) from said mandrel (1) ; and separating said layer from said mandrel (1); characterised by moving said strip (5) through at least one subsequent bath (7) in which electrodeposition of metal takes place on both sides of said strip (5) while it is moved through said subsequent bath (7), applying a current density of at least 10 A/dm2 and up to 300 A/dm2 to the conductive surface of the moving mandrel (1) and to the metal surface of the strip (5) in each of the subsequent baths (7,10, 11) ; and directing a forced flow of electrolyte onto the surface of the layer and said strip (5), wherein the reusable conductive pattern of the surface of the mandrel (1) takes the form of at least one battery electrode and the electrolyte contains additives suited specifically to permit combining a high rate of deposition with controlled surface roughness and controlled composition of the deposit. |
| 2. | A process according to claim 1, further characterised by applying a specified current density to induce a surface roughness in the range of Ra = 3 pm to Ra = 100 urn according to ISO 4287. |
| 3. | A process according to claim 1 or 2, characterised by modifying the electrolyte and the deposition conditions in each of said subsequent baths (7,10, 11) according to a desired layer structure to form multilayer products. |
| 4. | A process according to any of claims 1 to 3, characterised by supplying hardening dispersoid particles to the electrolyte in said first bath (2). |
| 5. | A process according to any of claims 1 to 4, characterised by providing alloying elements in the electrolyte of said subsequent baths (7,10,11) to provide corrosion resistance to the layers formed therein. |
| 6. | A process according to any of claims 1 to characterised by supplying hardening additives to the electrolyte in said subsequent baths (7,10,11). |
| 7. | A process according to any of the preceding claims, characterised in that additives are selected from the polyaromaticaliphatic class containing one or more oxo and/or hydroxyand/or ketogroups per molecule. |
| 8. | A process according to any of the preceding claims, characterised in that the molecular mass of the additives is between 300 and 1000. |
| 9. | A process according to claim 7, characterised in that the aliphatic chain contains at least 4 to 8 Catoms. |
| 10. | A process according to any of the preceding claims, characterised in that the electrolyte contains a combination of at least two different additives with different molecular weight and polarity. |
| 11. | A process according to any of the preceding claims, characterised in that the current density applied is in the range from at least 20 A/dm2 to 300 A/dm2. |
| 12. | A process according to any of the preceding claims, characterised in that the current density applied is in the range from at least 40 A/dm2 to 300 A/dm2. |
| 13. | A process according to any of the preceding claims, characterised by directing the forced flow of the electrolyte by forcing it through a multitude of nozzles onto the surface of said mandrel (1). |
| 14. | A process according to any of the preceding claims, characterised by directing the forced flow of the electrolyte by forcing it through a multitude of nozzles onto the surface of said strip (5). |
| 15. | A mandrel to be used in the process according to any of claims 1 to 13, comprising the shape of a cylinder. |
| 16. | The mandrel as claimed in claim 15, characterised in that the surface of said mandrel (1) comprises a conductive pattern consisting of a conductive surface between parallelsided isolating borders along the circumference of said cylinder. |
| 17. | A mandrel according to claim 15, characterised in that the conductive pattern on the surface of said mandrel (1) has the structure of an electrode, preferably a battery grid, or the structure of a current optimized electrode design. |
| 18. | A mandrel as claimed in any of claims 15 to 17, characterised in said the conductive area of the surface of said mandrel (1) is structured in the direction normal to the surface to form grooves, hillocks or the like which are transferred to the product during the forming process. |
| 19. | A process according to any of the preceding claims in which any of the anodes (3,8) in any of the baths consists of lead scrap. |
| 20. | A process according to any of the preceding claims in which any of the anodes (3,8) in any of the baths consists of remelted lead scrap. |
DE 44 04 817 Cl describes a process to manufacture battery grids by electroforming. However, the discontinuous process claimed there is limited to a production of individual grids on a plate-shaped cathode. Such a process is difficult to control and is not sufficiently economical. Furthermore, modern technology of battery plate production has changed over to a continuous process. It requires that the electrodes are provided in the form of an"endless"strip-shaped feed
material of electrodes connected to each other. Any new process which is to provide competitive or superior productivity and product properties will have to satisfy the requirements of the continuous plate making process.
Electrodeposition processes to produce metal continuously as a strip in sheet or foil form have been known for a long time.
US 1,567,079 discloses a continuous electrolytic process of forming sheet cathodes comprising the initial formation of a single sheet cathode on a horizontally moving, vertically disposed surface in a winding direction, then parting the cathode from the moving surface in an unwinding direction without interrupting the electrodeposition, then interrupting the deposition and then continuing the deposition upon the initially formed cathode, as it is moved horizontally in a vertical plane, whereby a plurality of sheet cathodes will be formed upon the surface of the cathode initially formed.
DE 585 633 uses a horizontal cylinder in a similar process.
DE 197 38 513 Cl relates to a process for producing a metal foil consisting of plural metals where different electrolyte baths are used.
US 4,169,018 discloses a process for electroforming thin copper foil on aluminum carrier material for use in printed circuits wherein a continuous strip of aluminum material is prepared by etching and rinsing steps, whereupon the prepared carrier material is passed through a single preselected composition copper plating bath having nitrate ions in the concentration of between 3 and 30 grams/liter and fluoride ions in the concentration of between 0.05 and 10 grams/liter.
This bath is operated at a constant, predetermined cathode
current density of between about 5.5 and 33 A/dm2 (50 and 300 A/foot2).
US 5,236,572 which has been used to formulate the preamble part of patent claim 1 discloses a method for continuously manufacturing parts requiring precision micro-fabrication. A surface of a mandrel having a reusable pattern thereon is moved through an electroforming bath. While the mandrel surface moves through the bath, a metal layer is deposited on the mandrel surface to define a pattern. After the metal layer has been deposited to the selected thickness, the metal layer is separated from the mandrel surface.
It is the object of the invention to provide a continuous electroforming process of high productivity and flexibility which satisfies the economical and technical demands for the product. This object is solved by the process as defined in claim 1.
The aim of the invention is to achieve a high rate of formation and, thus, a more economical process, and moreover a more highly optimized product than that obtained by previous technology. Such an optimized product is obtained because the process provides a high degree of flexibility in producing electrodes of different design, different layered composite structure and different surface structure.
The process of claim 1 is characterized by moving said strip through at least one subsequent bath in which electrodeposition of metal takes place on both sides of said strip while it is moved through said subsequent bath, applying a current density of at least 10 A/dm2 and up to 300 A/dm2 to the conductive surface of the moving mandrel and to the metal surface of the strip in each of the subsequent baths ; and directing a forced flow of electrolyte onto the surface of the layer and said strip, wherein the reusable
conductive pattern of the surface of the mandrel takes the form of at least one battery electrode and the electrolyte contains additives suited specifically to permit combining a high rate of deposition with controlled surface roughness and controlled composition of the deposit.
Preferably, the current density is specified to induce a surface roughness in the range of Ra = 3 urn to Ra = 100 um according to ISO 4287. Preferred current density ranges are from at least 20 A/dm2 to 300 A/dm2 and further preferred from at least 40 A/dm2 to 300 A/dm2.
In its simplest embodiment, only one subsequent bath is provided, however, it is possible to add further subsequent baths and to modify the electrolyte in each of said subsequent baths and the deposition conditions according to a desired layer structure to form multi-layer products.
Hardening dispersoid particles can be added to the electrolyte in said first bath and/or in said subsequent baths. Further, alloying elements can be included in the electrolyte of the subsequent baths to provide corrosion resistance and additional hardening to the layers formed therein.
The additives are selected from the polyaromatic/aliphatic class containing one or more oxo-and/or hydroxy-and/or keto-groups per molecule. The molecular mass of the additives may be in the range of about 300 to 1,000. The aliphatic chain should contain at least 4 to 8 C-atoms. It is preferred that the electrolyte contains a combination of at least two additive different substances with different molecular weight and polarity.
In the field of electrode position different types of additives, as referred to above, are applied such as dispersoid particles serving to harden the electrodeposited
structure, further alloying elements serving to improve the corrosion resistance and/or hardness, and additives in a narrower sense which control the surface, microstructure and the incorporation of the other additives.
An essential feature of the invention is the provision of a forced flow of electrolyte onto the surface of the layer on the mandrel and the strip. The forced flow can be generated by forcing the electrolyte through a multitude of nozzles onto the surface of said mandrel or the layer on the mandrel, respectively, and onto the surface of the strip.
A specific mandrel should be used in the process of the invention which advantageously comprises the shape of a cylinder. A conductive pattern is provided on the surface of the mandrel which may consist of a conductive surface between parallel-sided isolating borders along the circumference of the cylinder. The conductive pattern may, alternatively, have the structure of an electrode, preferably a battery grid, similar to that described in DE 44 04 817 C1, or the structure of a current optimized grid design. It is further preferred to structure the conductive area of the surface of the mandrel also in the direction normal to the surface to form grooves, hillocks or the like which are transferred to the product during the forming process.
It is also preferred to use in the process of the invention anodes in any of the baths that consist of lead scrap or of remelted lead scrap. Thereby, refining of the lead is advantageously combined with the production of battery electrodes as an immediate combination of two process steps which normally would be performed separately. An inventive step is even seen in this novel combination.
The invention will now be further explained with reference to the drawing, where the single figure schematically shows an
apparatus with which the continuous electroforming process of the invention can be carried out. The figure only shows the major parts of the apparatus. A mandrel 1 which is structured on its surface into a pattern of conductive and non- conductive areas, according to the design of the electrode shaped to be produced, is used as the cathode of an electrodeposition bath 2 with an anode 3. While the mandrel 1 is rotating, the metal deposite is forming and growing in thickness. After having reached sufficient resistance against tearing, corresponding to a specified thickness of the layer on the surface of mandrel 1, the layer is separated at a position 4 in strip shape 5 and is guided by guide and contact rolls 6 into the first subsequent bath 7 with anodes 8 and a submerged guide roll 9. Further subsequent baths such as 10,11 essentially have the same parts.
The process permits to produce electrodes with low thickness, e. g. 50 to 500 um, which are porefree and fully optimized in design and properties.
Example To produce battery grids having a size of 15 cm x 15 cm and a grid area fraction of 50 % of the grid size, the surface of a cylinder serving as the mandrel having a diameter of 1 m and a length of 1.2 m is provided with conductive areas corresponding to the grid structure. The cylinder is submerged into an electrolyte as disclosed in DE 44 04 817 Cl and rotates with a circumferential velocity of 106.8 m/h. The electrodeposition occurs at the surface of the cylinder at a current density of about 80 A/dm2. A lead grid strip forms on said cylinder and is separated therefrom upon reaching a layer thickness of 80 um. Subsequently the strip is transferred to a second electrolyte bath having an effective length of 33 m and is brought to the desired final thickness of 0.5 mm by electrodeposition on both surfaces of the strip
at a current density of 20 A/dm2. The production rate is 95 grids per minute.
The features disclosed in the foregoing description, in the claims and/or in the accompanying drawing may, both separately and in any combination thereof, be material for realising the invention in diverse forms thereof.