Anti-Tarnish Treatment of Metal Foil

FIG. 1 is schematic representation of a system for treating foil in accordance with the present invention.

As previously noted, the present invention involves an improved technique for treating copper and copper alloy foil materials to improve tarnish resistance. As used herein, the term copper and copper alloy foil includes copper and copper base alloy sheet or strip foil and slab materials.

The particular process to be described herein is useful with electrodeposited or wrought foil and particularly useful for either types of foil which have one surface which has been provided with a dendritic or nodular roughening treatment such as described in U.S. Pat. No. 4,468,293.

In accordance with a preferred embodiment of the invention, the foil is electrodeposited foil of which one side (the outside surface) has been subjected to a dendritic or nodular roughening treatment of the type disclosed U.S. Pat. No. 4,468,293. After such dendritic or nodular surface treatment, the foil 10 may be immediately processed in accordance with the present invention, or the foil stored on a takeup roll 12 from which it may be fed to the treatment line.

The foil 10, whether electrodeposited or wrought, may be rinsed with deionized water at a rinse station 14 and then passed by means of a series of rolls 16, 18, 20 and 22 through a zinc plating treatment tank 24 containing an appropriate zinc plating solution 26 therein. This treatment may be used to apply a relatively heavy coating of zinc to the rough side of the foil 10 while a thin coating of zinc is applied to the smooth of the foil. The thin layer of zinc on the smooth side is in the order of from about 0.001 to about 0.06 mg/cm.sup.2. The heavy coating of zinc may be between about 0.3 to about 3.0 g/m.sup.2 and preferably between about 0.5 to about 2.0 g/m.sup.2.

The zinc plating solution 26 comprises a suitable form of zinc, preferably in the form of zinc sulfate. The zinc sulfate is dissolved in water to form an aqueous solution of from about 0.1M to about 1.5M. The zinc deposit is greater on the roughened side of the foil as compared with the smooth side. This may be accomplished in a number of ways. One such way includes rendering cathodic by electrically connecting one or more rolls to the negative terminal of a suitable power supply 28. Two separate sets of anodes 30 and 32 may be used, one set 30 facing the smooth side of the foil and the second 32 facing the roughened or dendritic side of the foil. The anodes 30 and 32 are connected to positive terminals of the power supply 18 which provides the proper current density.

The current density applied to the front side of the foil may be between 5 to about 150 mA/cm.sup.2 and preferably around 40 mA/cm.sup.2 while the current density applied to the back or smooth side of the foil is from about .01 to about 100 mA/cm.sup.2 and preferably around 5 mA/cm.sup.2. To provide for the thicker layer on the roughened side as compared with the smooth side, in addition to using a higher current density, the length of time at which the front surface of the foil 10 may be subjected to the plating treatment may be longer than the back. This can be accomplished in a variety of ways, one of which is by having the length of the anodes 32 facing the roughened side longer than the anodes 30 on the smooth side. With the temperature of the plating solution in the range of about 35 to 40.degree. C., the current density may be applied to the front side in the order of from about 2 to about 100 seconds and preferably 10 seconds while the current density may be applied to the back side in range from about 0.1 to about 100 seconds and preferably about 5 seconds.

After the zinc plating treatment, the foil 10 may pass through a rinse station 34 wherein it is rinsed in deionized water. The rinse station 34 may include a plurality of spray nozzles (not shown) arranged to spray deionized water on both sides of the foil 10. While such nozzles may be arranged in any suitable configuration and may have any desired nozzle pattern it is preferred that the nozzles be arranged in banks of adjacent square pattern nozzles on opposite sides of the foil 10. Alternatively, the rinse station 34 may comprise a tank containing the rinse solution and through which the foil is passed or a combination of sprays and immersion.

After the rinse station 34, the foil 10 is immersed in a tank 36 containing a chromic acid-sulfuric acid solution 38. The foil is passed through the tank 36 by means of suitable rolls 40, 42, 44 and 46. In accordance with the present invention, the solution 38 in the tank contains chromic acid in a concentration of about 0.02 grams per liter (hereinafter g/1) to about 1.0 g/1 and sulfuric acid in the concentration in the range of about 0.02 g/1 to about 20 g/1 depending upon the temperature and length of time of treatment. Generally the solutions contain no other constituents besides water and some minor impurities. Preferably, the solution consists essentially of from about 0.1 g/1 to about 0.3 g/1 of chromic acid, from about 0.02 to about 0.7 g/1 of sulfuric acid and the balance essentially water.

While the foil may be treated with the chromic acid-sulfuric acid solution at any desired temperature, it is preferred that the solution 28 in the tank be maintained at an elevated temperature in the range of 50.degree. to 55.degree. C. With this temperature and the concentrations of chromic acid being 0.2 g/1 and the sulfuric acid being 0.05 g/1, the foil may be immersed in the solution for about 20 seconds.

It has been found that the use of sulfuric acid in this step enhances the reaction of the Cr.sup.+6 with the metal surface and does not have a deleterious reaction with the zinc layer. If phosphoric acid is used in place of the sulfuric acid, although relatively good tarnish resistance is provided, the resulting foil has a relatively inferior peel strength believed to be caused by the chemical reaction of the zinc, sulfuric acid and calcium hydroxide used in the next step.

After treatment of the foil 10 with the chromic acid-sulfuric acid solution, the foil 10 may be further treated by immersion in a tank 48 containing a dilute basic solution 50 having a pH greater than about 8. A plurality of rolls 52, 54, 56 and 58 may be used to define the path by which the foil 10 passes through the tank.

Dilute basic solutions in accordance with the present invention comprise aqueous solutions having a pH of at least 8. Solutions of particular benefit are those having a pH in the range of about 9 to 11.5. Any suitable addition agent may be employed to adjust the pH of this solution. Generally, the addition will be selected from the group consisting of the salts of alkali metals, the salts of alkaline earth metals, the hydroxides of the alkali metals, and the hydroxides of the alkaline earth metals. A preferred addition agent is selected from a group consisting of sodium hydroxide, calcium hydroxide, potassium hydroxide and ammonium hydroxide. While the amount of addition agent present in the solution will be a function of the desired pH level for the solutions, generally the addition agent will be present in the concentration of greater than 1 ppm and preferably about 50 ppm.

The temperature of the basic solution may be maintained at a temperature in the range from room temperature to about 100.degree. C. and preferably between about 45.degree. to about 50.degree. C. While the time of immersion of the foil in the basic solution may vary from about 1 second to about 120 seconds, most preferably it is immersed for about 5 seconds to about 30 seconds. It has been found that the use of the basic rinse solution after treatment with the chromic acid-sulfuric acid bath serves to enhance the anti-tarnish treatment.

After the foil 10 exits from the tank 48 containing the basic rinse solution, it passes through a drying station 60, positioned between the roll 58 and roll 62. Numerous drying processes which may be used are well known in the art. One such process which may be used embodies a water blow-off stage followed by a hot air tunnel drying stage. An alternative process which may be used utilizes heated blow-off air for both bulk and evaporative water removal. In this latter process, the hot air can be directed against the foil when it is lying on drum rolls in the line. In still another alternative process, at least one internally heated drum roll or infra-red heating may be used to dry the foil. Any of these drying processes may be incorporated into the drying station 60. After the drying station 60, the foil may be wound onto a take up reel 64.

By virtue of the above described treatment, copper or copper alloy foil materials may be provided which possess good tarnish resistance and have good peel strength when bonded to a substrate material.

The U.S. Patents described in the specification are intended to be incorporated herein by reference in their entirety.

While the invention has been described above in connection with specific embodiments thereof, it is evident that many alternations, modifications, variations will be apparent to those skilled in the art in view of the foregoing description. Accordingly, it is intended to embrace all alternatives, modifications and variations as fall within the spirit and broad scope of the appended claims.