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Publication numberUS3767537 A
Publication typeGrant
Publication dateOct 23, 1973
Filing dateNov 8, 1971
Priority dateNov 8, 1971
Publication numberUS 3767537 A, US 3767537A, US-A-3767537, US3767537 A, US3767537A
InventorsSelker M
Original AssigneeGould Inc
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Method and apparatus for continuous production of nickel foil
US 3767537 A
A method and apparatus for continuously producing pure, solid, and pore-free nickel foil by electrodeposition, utilizing a cathode drum of titanium.
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Description  (OCR text may contain errors)

United States Patent Selker Oct. 23, 1973 METHOD AND APPARATUS FOR [58] Field of Search 204/12, 13, 281, CONTINUOUS PRODUCTION OF NICKEL 204/208, 216

FOIL [75] Inventor: Milton L. Selker, Shaker Heights, [56] References cued Ohio UNITED STATES PATENTS 3,461,046 8/l969 Clancy 204/13 [73] l Chlcago 2,646,396 7 1953 Dean 204/12 [22] Filed: Nov. 8, 1971 Primary Examiner-T. Tufanello 21 A l. N 196,332 1 pp 0 Attorney-Edward E. Sachs Related US. Application Data [63] Continuation-impart of Ser. No. 836,822, June 26, [57] ABSTRACT 1969 abandoned A method and apparatus for continuously producing pure, s olid, and pore-free nickel foil by electrodepo- [52] U.S. Cl 204/13, 204/208, 220041221861, Sition, utilizing a Cathode drum of titanium [51] Int. Cl C23b 7/02, B )lk 1/00, B23n 1/00 4 Claims, 1 Drawing Figure IIIIIIYIIIIIIII I!!! n METHOD AND APPARATUS FOR CONTINUOUS PRODUCTION OF NICKEL FOIL This application is a continuation-impart of my US. Pat. application, Ser. No. 836,822, filed June 26, 1969, and now abandoned. I

The present invention relates generally to a method using an improved apparatus for continuously producing nickel foil by electrodeposition.

Nickel foil enjoys some specialized use in printed circuitry because of the strength, high temperature stability, and ease of welding nickel metal to itself and other components of the printed circuit. To be so used, the nickel foil must satisfy some certain requirements such as purity, homogeneous crystallinity, evenness, and absence of porosity. While purity of the foil can be attained with relative ease, its even and/or non-porous surface has been difficult to accomplish because of its direct relationship with the cathode surface.

Heretofore, plating devices for producing electroformed nickel foil have utilized mandrels comprising stainless steel drums or steel drums plated with thin layers of copper, nickel, and chromium, respectively. In each case, the exterior surface of the drum must be kept highly polished.

Generally, the plating solution and the plating process will cause cracks, pits, and/or imperfections on the drums surface which becomes unsuitable for nickel foil production. It is necessary, therefore, to stop production periodically to maintain the high polish on the drum. Such stoppages are quite costly as they can occur every few weeks.

It is a principal object of the present invention to provide an apparatus for the continuous production of pure and pore-free nickel foil.

A further object of the invention is to provide a platin g drum on which pure and pore-free nickel foil is continuously electrodeposited, said drum being essentially maintenance free.

A cathode drum comprising in part a relatively thin titanium metal cylinder has been suggested in the past, see French Pat. No. 1,540,378, for making copper foil. The drum includes a support structure of lead arranged in close proximity to the titanium cylinder. The lead support constitutes a lining having a greater coefficient of expansion than titanium to provide close contact between the two surfaces at the operating temperature. According to the patent this is required to provide a uniform current distribution, by way of the lead lining, through the titanium cylinder.

The titanium cylinder and the supporting structure of the above-mentioned French patent must be machined to very close tolerances in order to provide electrical contact throughout the drum surface. The temperature of the bath must be kept at such a relatively high level so that the contact between the two cylinders, due to expansion, is maintained. While such requirements may be satisfactory for the production of copper foil, they are not desirable for the production of nickel foil.

It has been found that the difficulties of evenly distributing the current across a titanium drum is related to the axial length of the drum and these difficulties can be removed and sufficient electrical conductivity can be established by keeping the drum to a minimum dimension as disclosed herein. This eliminates the need for a conductor lining as suggested in the above Patent and thus avoids problems of lead contamination.

For a better understanding of the present invention, together with other and further objects thereof, reference is had to the following description taken in connection with the accompanying drawings, and its scope will be pointed out in the appended claims.

The single FIGURE drawing shows an elevational view partly in section of an apparatus for electrodeposition.

Referring to the accompanying drawing, there is shown an end view of the plating apparatus wherein the cathode drum 10 is mounted to rotate in plating solution 12, bearings and driving mechanism not shown. The cathode drum may be of any suitable diameter and length depending on the particular size of nickel foil desired. A drum of about four feet in diameter and 24 inches long has been found particularly suitable. A tank 14 holds the plating solution 12 in contact with the bottom half of cathode drum 10. Washing, cleaning, and drying devices, not shown, are normally mounted on the tank 14 or in the proximity thereof. Conforming anodes 16 are closely situated to the cathode drums exterior surface and are held by supporting units 18 which extend axially the full length of the drum. Pure metallic nickel chips and pieces comprise the anodes which are generally covered by a diaphragm 20 comprising a permeable cloth acting as a filter to prevent small anode particles from causing a rough plate. This diaphragm 20 can be of any suitable material such as muslin cloth. Also mounted in the tank 14 is a piping system 22 which, by pump action, circulates rapidly the plating solution in the direction of the arrows between the drum and the anode, thus maintaining agitation and concentration of said plating solution.

The drum 10 is rotatably mounted about a central shaft 26, supported by a bearing 28 at each axial end, and carrying at each such end a current collector ring 30. An electron potential source conducts current to the rings 30 from which the current passes radially through drum end plates (not shown) into drum 10. A

suitable conventional foil take-up reel (not shown) may.

be mounted on a frame 24 and may be mechanically linked to the shaft 26.

The cathode drum constitutes the most essential feature of the plating apparatus, and I have found that a drum made out of titanium metal or its alloys has been particularly advantageous in the production of pure, solid, and pore-free nickel foil. Moreover, the titanium drum has been found to require essentially no maintenance over a period of about one year, thus eliminating the disadvantages of periodic stoppages necessary with prior art drums.

The titanium cathode drum of the present invention is a unitary, self-supporting structure, preferably made from a solid titanium billet of suitable dimensions. By the piercing and ring-rolling process, the billet attains a cylindrical shape having a continuous solid surface. After attaining the proper size and thickness the drum is then machined and polished by suitable means. Because of the high chemical resistance of titanium metal and/or its alloys, the finished polish on the surface can be maintained over a long period of time compared to that of stainless steel or chrome-plated steel drums. The ring-rolled, seamless titanium drum presents the advantage of having a weld-free surface. Generally, welds used in manufacturing drums are of different hardness and crystal structure than the parent metal and consequently will receive a different luster or appearance during polishing operation. This difference in appearance will be imparted to the nickel foil which becomes commercially undesirable. Furthermore, the welded areas may be porous, which would render the nickel foil correspondingly porous and thus unacceptable for printed circuit use.

As to the electrolytic bath used, it is preferably of the nickel sulfamate type which comprises 120 g/l nickel metal, 40 g/l boric acid, 7.5 g/l nickel chloride hexahydrate, and 0.05 percent of anti-pit additive. The pH is preferably in the range of 3.9 to 4.1 and the operating temperature between 5055 C. To produce a nickel foil having 2 mil thickness and utilizing a current density of 135 asf, the surface speed of the drum is 4 inches per minute. Similarly, for 1 mil thickness, the speed is doubled, i.e., 8 inches per minute. The ring-rolled, seamless drum is preferably of sufficient thickness to be self-supporting, i.e., a thickness of over three-eighths of an inch is satisfactory. The polishing of the drums surface is accomplished by machining. The final, smooth finish is effected via abrasive belt finishing techniques utilizing belts coated with silicon carbide particles. Other polishing agents can be used, however.

For continuous operation and free maintenance, it is essential that the drums surface is not injured or bruised, although minor and shallow scratches are not very critical as they can be removed by simple machining and/or polishing operation.

The titanium drum needs no protective coating in or out of operation. It is believed that a thin layer of oxide which forms on the drums surface serves, firstly, as a means or protection and, secondly, as a means of allowing the nickel foil layer to strip off the drum with ease.

It has been found that a ring-rolled, seamless drum made of a titanium alloy comprising essentially 6 percent aluminum, 4 percent vanadium, and the balance titanium, and known as 6 Al-4V titanium alloy, is very satisfactory as a maintenance-free cathode drum. This 6 Al-4V-Ti drum has operated continuously for one year without any sign of deterioration or need of maintenance.

It is to be understood that the present invention is not limited to the precise construction, as herein discribed and illustrated, but embraces all such variations and modification as are within the scope of the invention as set forth in the following claims.

What is claimed is:

1. A method for making nickel foil from an electrolytic solution comprising thesteps of:

placing a solution of nickel compounds into a tank to partially immerse the outside surface of a cathode drum mounted for rotation in said solution and having a unitary, seamless, self-supporting circumferential surface composed exclusively of titanium or an alloy thereof;

providing a nickel anode in said solution which conforms to and is in proximity with an immersed portion of said cylindrical surface;

electrically energizing the cathode;

rotating the drum while agitating the solution to plate a film of nickel on said surface; and

stripping said film from said surface.

2. A method according to claim 1 including the step of filtering small nickel particles which may pass from said anode to said cathode.

3. A method for making a nickel foil from an electrolytic solution comprising the steps of:

placing a solution of nickel compounds into a tank;

continuously passing outside surface portions of a unitary, seamless, self supporting, titanium or titanium alloy cathode drum into and out of said solution;

providing a nickel anode in said solution which conforms to and is in proximity with immersed portions of said surface portions;

electrically energizing the cathode;

agitating the solution; and

stripping nickel foil from said surface.

4. A method according to claim 3 including the step of filtering small nickel particles which may pass from said anode to said cathode.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2646396 *Mar 17, 1949Jul 21, 1953Dean Reginald SMethod of making electroformed articles
US3461046 *May 6, 1966Aug 12, 1969Anaconda CoMethod and apparatus for producing copper foil by electrodeposition
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3859194 *Feb 13, 1974Jan 7, 1975Electricity CouncilElectrodeposition apparatus
US4240894 *Oct 5, 1979Dec 23, 1980Edward AdlerDrum for electrodeposited copper foil production
US4530739 *Mar 9, 1984Jul 23, 1985Energy Conversion Devices, Inc.Method of fabricating an electroplated substrate
US4565607 *May 16, 1985Jan 21, 1986Energy Conversion Devices, Inc.Method of fabricating an electroplated substrate
US4921590 *Mar 27, 1989May 1, 1990Yates Industries, Inc.Production of metal foil having improved weight distribution across the width of the foil
US5228965 *Oct 30, 1990Jul 20, 1993Gould Inc.Method and apparatus for applying surface treatment to metal foil
US5360525 *Mar 16, 1993Nov 1, 1994United Foils Inc.Apparatus for making metal foil
US5393396 *Oct 30, 1990Feb 28, 1995Gould Inc.Apparatus for electrodepositing metal
US5712046 *Jul 3, 1996Jan 27, 1998Sumitomo Metal Industries, Ltd.Titanium ring for an electrodeposition drum and a method for its manufacture
EP0154555A2 *Mar 7, 1985Sep 11, 1985Energy Conversion Devices, Inc.Electroplated substrate
EP1447462A1 *Feb 14, 2003Aug 18, 2004Future Metal Co., Ltd.Apparatus and method for fabricating metal fibres using electroforming
WO1990008208A1 *Jan 16, 1990Jul 26, 1990Square D CoElectroplating drum cathode with high current-carrying capability
WO1995025833A1 *Mar 24, 1994Sep 28, 1995David E DykeApparatus for making metal foil
WO1998036107A1 *Feb 13, 1998Aug 20, 1998Dover Ind Chrome IncPlating apparatus and method
U.S. Classification205/77, 204/208, 204/281, 204/216
International ClassificationC25D1/04
Cooperative ClassificationC25D1/04
European ClassificationC25D1/04