Heat-treatable chromium

• US 5,413,646 A
• Filed: 03/16/1993
• Issued: 05/09/1995
• Est. Priority Date: 02/08/1991
• Status: Expired due to Term

• Current Assignee: Oregon Tool Incorporated, State Of Oregon Acting By And Through The State Board Of Higher Education On Behalf Of Portland State University
• Original Assignee: Blount Incorporated (Oregon Tool Incorporated)
• Inventors: Dash, John, DeHaven, John
• Primary Examiner(s): Niebling, John
• Assistant Examiner(s): Leader, William T.
• Application Number:
  US08/033,635
• Time in Patent Office: 784 Days
• Field of Search: 205/227, 205/243, 205/287, 205/255, 205/259, 205/289, 148/518
• US Class Current: 148/518
• CPC Class Codes: C25D 3/06 from solutions of trivalent chromium
• CPC Class Codes: C25D 5/50 by heat-treatment

Abstract

A method for depositing chromium and iron metals on substrates is disclosed in which the chromium hardens when heated. The electrolytic plating bath preferably includes: (a) water soluble Cr(III) produced by reducing Cr(VI) with sufficient amounts of methanol or formic acid; (b) ammonium formate; (c) a sulfate catalyst, such as sodium sulfate; (d) an inorganic iron compound, such as iron sulfate; (e) sufficient amounts of boric acid to substantially saturate the bath; and (f) a sufficient amount of sulfuric acid to provide a bath pH of from about 1.0 to about 1.5. The heat-hardenable chromium deposit allows the plated substrate to be heat tempered after plating to provide a KHN of greater than about 1200. This eliminates the necessity of removing oxidation products from an unplated heated substrate. Moreover, the amount of toxic Cr(VI) present in the bath is greatly diminished, and is replaced with a Cr(III) species that is environmentally safer. Electrolytic plating baths of the present invention having ammonium formate and a total sulfate concentration of about 140 g/L to about 180 g/L produce chromium and iron metal deposits on substrates having thicknesses of up to about 160 μm. Moreover, the iron content of the deposit can be varied over a range of from about 10% to about 90% by adjusting the sulfate-to-iron ratio in the plating bath.

Claims

1. A method for electroplating a workpiece, comprising:

providing a plating bath comprising (a) trivalent chromium produced by reducing a Cr(VI) compound to Cr (III) with methanol or formic acid, (b) ammonium formate, (c) an inorganic iron compound, (d) a sulfate catalyst, and (e) a sufficient amount of sulfuric acid to provide a bath pH of from about 0.5 to about 1.5, wherein the bath being maintained substantially free of hexavalent chromium ions by the addition of sufficient amounts of methanol or formic acid;

providing an anode in the plating bath;

placing the workpiece in the bath to act as a cathode;

electroplating a chromium and iron metal layer onto the workpiece by passing an electric current through the plating bath; and

heating the workpiece from about 600°

F. to about 1675°

F. for a sufficient period of time to harden the workpiece while retaining or increasing hardness of the chromium alloy plated on the workpiece.

2. The method according to claim 1 wherein the total sulfate concentration is from about 140 g/L to about 180 g/L.

3. The method according to claim 2 wherein the total sulfate concentration is about 165 g/L.

4. The method according to claim 2 wherein the total sulfate concentration includes sodium sulfate at a concentration of from about 35 g/L to about 60 g/L.

5. The method according to claim 1 wherein the plating bath further includes a sufficient amount of boric acid to increase the brightness of the deposit.

6. The method according to claim 5 wherein the plating bath is saturated with boric acid.

7. The method according to claim 6 wherein the bath consists essentially of from about 28 g/L to about 35 g/L trivalent chromium, from about 10 g/L to about 12 g/L inorganic iron compound, from about 21 g/L to about 26 g/L ammonium formate, from about 140 g/L to about 180 g/L total sulfate concentration wherein about 35 g/L to about 60 g/L is contributed by sodium sulfate, a sufficient amount of boric acid to substantially saturate the bath, and a sufficient amount of sulfuric acid to provide a bath pH of from about 1.0 to about 1.5.

8. The method according to claim 1 wherein the bath comprises from about 28 to about 35 g/L trivalent chromium, from about 10 to about 12 g/L inorganic iron compound, from about 21 to about 26 g/L ammonium formate, and from about 140 g/L to about 180 g/L total sulfate of which from about 35 g/L to about 60 g/L is contributed by sodium sulfate.

9. The method according to claim 8 wherein the bath comprises about 31.5 g/L trivalent chromium, about 11.4 g/L iron sulfate, about 23.4 g/L ammonium formate, and about 37 g/L sodium sulfate.

10. The method according to claim 1 wherein the step of electroplating comprises providing a current density of from about 0.8 to about 6.5 A/in².

11. The method according to claim 1 wherein the step of heating the workpiece comprises heating the workpiece from a temperature of from about 600°

to about 1000°

F.

12. The method according to claim 1 wherein the workpiece is a cutter.

13. The method according to claim 1 wherein the step of electroplating comprises electroplating the workpiece with a chromium and iron metal layer having a thickness of up to about 160 μ

m.

14. The method according to claim 1 wherein the amount of iron deposited can be determined from a percentage of from about 10% iron to about 90% iron by adjusting the amount of iron in the bath.

15. A method for plating a workpiece, comprising the steps of:

providing a plating bath comprising (a) from about 28 g/L to about 35 g/L trivalent chromium produced by reducing a Cr(VI) compound to Cr(III) with methanol or formic acid, the bath thereafter being substantially free of hexavalent chromium ions, (b) from about 10 g/L to about 12 g/L of iron introduced by an inorganic iron compound, (c) from about 21 g/L to about 26 g/L ammonium formate, (d) from about 140 g/L to about 180 g/L total sulfate wherein the total sulfate concentration includes a sufficient amount of sulfuric acid to provide a bath pH of from about 0.5 to about 1.5;

providing an anode in the plating bath;

placing a workpiece in the bath to act as a cathode;

electroplating a chromium and iron metal layer onto the workpiece by passing an electric current through the bath; and

heating the workpiece from about 600°

F. to about 1675°

F. for a sufficient period of time to harden the workpiece while retaining or increasing hardness of the chromium alloy plated on the workpiece.

16. The method according to claim 15 wherein the total sulfate concentration includes iron sulfate, sodium sulfate, and sulfuric acid, and the total sulfate concentration is from about 140 g/L to about 180 g/L.

17. The method according to claim 16 wherein the bath is saturated with boric acid.

18. The method according to claim 17 wherein the bath comprises about 31.5 g/L trivalent chromium, about 11.4 g/L iron sulfate, about 23.4 g/L ammonium formate, and about 37 g/L sodium sulfate.

19. The method according to claim 18 wherein the step of electroplating comprises plating the workpiece with a chromium and iron metal layer having a thickness of up to about 160 μ

m.

20. A method for electroplating a workpiece, comprising the steps of:

providing a plating bath comprising (a) about 31.5 g/L trivalent chromium produced by reducing a Cr(VI) compound to Cr(III) with methanol or formic acid, the bath thereafter being substantially free of hexavalent chromium ions, (b) about 11.4 g/L iron sulfate, (c) about 23.4 g/L ammonium formate, (d) about 165 g/L total sulfate wherein the total sulfate includes amounts contributed by about 37 g/L sodium sulfate and a sufficient amount of sulfuric acid to provide a bath p H of from about 1.0 to about 1.5, and (f) a sufficient amount of boric acid to substantially saturate the bath with boric acid;

providing an anode in the plating bath;

placing a workpiece in the bath to act as a cathode; and

electroplating a chromium and iron metal layer onto the workpiece by passing an electric current through the plating bath wherein the layer has a thickness of from about 5 μ

m to about 160 μ

m, the layer exhibiting the property of maintaining or increasing its hardness when subjected to heat treatment at a temperature of from about 600°

F. to about 1675°

F.

21. The method according to claim 20 and including the step of heating the workpiece, after the step of electroplating, to a temperature of from about 600°

F. to about 1000°

F.

22. A method for electroplating a workpiece with a chromium and iron metal layer so that the iron concentration in the metal layer is from about 10 percent to about 90 percent, the method comprising the steps of:

providing a plating bath comprising (a) trivalent chromium compound produced by reducing Cr(VI) present in the bath to Cr(III) by the addition of sufficient amounts of methanol or formic acid, the bath thereafter being substantially free of hexavalent chromium ions, (b) an inorganic iron compound, (c) a sulfate catalyst, (d) ammonium formate, and (e) a sufficient amount of sulfuric acid to provide a bath pH of from about 0.5 to about 1.5, wherein the amount of iron in the bath is selected to provide the desired amount deposited in the layer;

providing an anode in the plating bath;

placing a workpiece in the bath to act as a cathode;

electroplating the workpiece with a chromium and iron metal layer having an iron concentration of from about 10 percent to about 90 percent by passing an electric current through the plating bath; and

heating the workpiece from about 600°

F. to about 1675°

F. for a sufficient period of time to harden the substrate while retaining or increasing hardness of the chromium alloy plated on the workpiece.

23. The method according to claim 22 wherein the bath further includes an amount of boric acid sufficient to substantially saturate the bath.

24. The method according to claim 22 wherein the layer has about 60% to about 90% chromium.

25. The method according to claim 22 and further including the step of heating the workpiece, after the step of electroplating, from a temperature of from about 600°

F. to about 1000°

F.

26. An electroplating bath for plating a metal article with a chromium alloy layer having a thickness of from about 5 μ

m to about 160 μ

m, the layer maintaining or increasing its hardness when subjected to heat treatment at a temperature of from about 600°

F. to about 1675°

F., consisting essentially of;

from about 28 g/L to about 35 g/L trivalent chromium produced by reducing Cr(VI) to Cr(III) by additions of sufficient amounts of methanol or formic acid, the bath thereafter being substantially free of hexavalent chromium ions;

from about 10 g/L to about 12 g/L inorganic iron compound;

from about 21 g/L to about 26 g/L ammonium formate;

from about 140 g/L to about 180 g/L total sulfate;

a sufficient amount of sulfuric acid to provide a bath pH of from about 0.5 to about 1.5; and

an amount of boric acid sufficient to substantially saturate the bath.

27. The bath according to claim 26 wherein the bath consists essentially of:

from about 28 g/L to about 35 g/L trivalent chromium produced by substantially completely reducing Cr(VI) to Cr(III) by the addition of sufficient amounts of methanol or formic acid;

from about 10 g/L to about 12 g/L iron;

from about 21 g/L to about 26 g/L ammonium formate;

from about 37 g/L to about 60 g/L sodium sulfate;

a sufficient amount of sulfuric acid to provide a bath pH of from about 0.5 to about 1.5, wherein the total sulfate concentration is from about 140 g/L to about 180 g/L; and

an amount of boric acid sufficient to substantially saturate the bath.

28. An electroplating bath for plating a metal article with a chromium alloy layer, the layer maintaining or increasing its hardness when subjected to heat treatment at a temperature of from about 600°

F. to about 1675°

F. consisting essentially of;

about 31.5 g/L trivalent chromium produced by reducing Cr(VI) to Cr(III) by adding to the bath sufficient amounts of methanol or formic acid, the bath thereafter being substantially free of hexavalent chromium ions;

about 11.4 g/L inorganic iron compound;

about 23.4 g/L ammonium formate;

about 37 g/L sodium sulfate;

a sufficient amount of sulfuric acid to provide a bath pH of about 1.0 to about 1.5; and

an amount of boric acid sufficient to substantially saturate the bath.