Gold plating composition and method

Claim 2

A gold plating bath comprising an aqueous solution of: A. 15-150 grams per liter of an alkali metal dihydrogen phosphate as the electrolyte; B. 15-150 grams per liter of nitrilotris(methylene) triphosphonic acid; C. a phosphate compound of a metal selected from the group consisting of nickel, cobalt and mixtures thereof, said compound providing 0.010-5.0 grams per liter of said metal calculated as the metal; D. 3-37.5 grams per liter of triethanolamine borate; E. alkali metal gold cyanide in an amount providing 2-17 grams per liter of gold calculated as the metal; and F. free alkali metal cyanide in an amount equal to at least 2.5 percent by weight of the gold metal and sufficient to prevent precipitation of the metal values, said solution having a pH of 3.8-4.5 and a specific gravity of 6°-22° Baume.

Claim 3

The gold plating bath in accordance with claim 1 wherein said phosphate compound is produced by the reaction of the carbonate salt of a metal selected from the group consisting of nickel, cobalt and mixtures thereof, with nitrilotris(methylene) triphosphonic acid.

Claim 4

The gold plating bath in accordance with claim 1 wherein said metal is cobalt.

Claim 5

The gold plating bath in accordance with claim 1 wherein said alkali metal phosphate is present in the amount of 40-60 grams per liter, said triphosphonic acid compound is present in the amount of 40-75 grams per liter, said metal phosphate compound provides the metal in the amount of 0.25-0.5 grams per liter and said triethanolamine borate is present in the amount of 5-15 grams per liter.

Claim 6

The gold plating bath in accordance with claim 4 wherein said alkali metal gold cyanide provides 7-10 grams per liter of gold metal and the alkali metal cyanide is present in the amount of 3.0-4.0 percent by weight of the gold metal.

Claim 7

In a method of electroplating hard gold deposits upon a workpiece, the steps comprising: A. immersing a workpiece having an electrically conductive surface in a gold plating bath comprising an aqueous solution of: 1. 15-150 grams per liter of an alkali metal dihydrogen phosphate as the electrolyte; 2. 15-150 grams per liter of nitrilotris(methylene) triphosphonic acid; 3. a phosphate compound of a metal selected from the group consisting of nickel, cobalt and mixtures thereof, said compound providing 0.010-5.0 grams per liter of said metal calculated as the metal; 4. 3-37.5 grams per liter of triethanolamine borate; 5. alkali metal gold cyanide in an amount providing 2-17 grams per liter of gold calculated as the metal; and 6. free alkali metal cyanide in an amount equal to at least 2.5 percent by weight of the gold metal and sufficient to prevent precipitation of the metal values, said solution having a pH of 3.8-4.5 and a specific gravity of 6°-22° Baume; B. maintaining the temperature of said bath at about 30°-60° C.; C. applying an electrical potential across said workpiece and an anode to provide a current density of about 0.1-20 amperes per square decimeter at said workpiece to effect the desired thickness for the electrodeposit; and D. removing the electroplated workpiece from said bath.

Claim 8

In a method of electroplating hard gold deposits upon a workpiece, the steps comprising: A. immersing a workpiece having an electrically conductive surface in a gold plating bath comprising an aqueous solution of: 1. 15-150 grams per liter of an alkali metal dihydrogen phosphate as the electrolyte; 2. 15-150 grams per liter of nitrilotris(methylene) triphosphonic acid; 3. a phosphate compound of a metal selected from the group consisting of nickel, cobalt and mixtures thereof, said compound providing 0.010-5.0 grams per liter of said metal calculated as the metal; 4. 3-37.5 grams per liter of triethanolamine borate; 5. alkali metal gold cyanide in an amount providing 2-17 grams per liter of gold calculated as the metal; and 6. free alkali metal cyanide in an amount equal to at least 2.5 percent by weight of the gold metal and sufficient to prevent precipitation of the metal values, said solution having a pH of 3.8-4.5 and a specific gravity of 6°-22° Baume; B. maintaining the temperature of said bath at about 30°-60° C.; C. applying an electrical potential across said workpiece and an anode to provide a current density of about 0.1-20 amperes per square decimeter at said workpiece to effect the desired thickness for the electrodeposit; and D. removing the electroplated workpiece from said bath.

Claim 9

The method of electroplating in accordance with claim 6 wherein said alkali metal phosphate is present in the amount of 40-60 grams per liter, said triphosphonic acid compound is present in the amount of 40-75 grams per liter, said metal phosphate compound provides the metal in the amount of 0.25-0.5 grams per liter and said triethanolamine borate is present in the amount of 5-15 grams per liter.

Claim 10

The method of electroplating in accordance with claim 7 wherein said alkali metal gold cyanide provides 7-10 grams per liter of gold metal and the alkali metal cyanide is present in the amount of 3.0-4.0 percent by weight of the gold metal.

Claim 11

The method of electroplating in accordance with claim 8 wherein the current density is 0.5-1.5 amperes per square decimeter.

Claim 12

The method in accordance with claim 6 wherein said metal phosphate compound is produced by the reaction of the carbonate salt of a metal selected from the group consisting of nickel, cobalt and mixtures thereof, with nitrilotris(methylene)triphosphonic acid.

Claim 13

The method of electroplating in accordance with claim 6 wherein the current density is 0.5-1.5 amperes per square decimeter.