Compositionally modulated zinc-iron multilayered coatings

Patent metadata

Field	Value
Publication number	US-10767274-B2
Application number	US-201715680326-A
Country	US
Kind code	B2
Filing date	Aug 18, 2017
Priority date	Jun 9, 2017
Publication date	Sep 8, 2020
Grant date	Sep 8, 2020

Abstract

The present disclosure provides electrolyte solutions for electrodeposition of zinc-iron alloys, methods of forming electrolyte solutions, and methods of electrodepositing zinc-iron alloys. An electrolyte solution for electroplating can include an alkali metal citrate, an alkali metal acetate, a citric acid, and glycine with a metal salt. An electrolyte solution can be formed by dissolving an alkali metal citrate, an alkali metal acetate, a citric acid, and glycine in water or an aqueous solution. Electrodepositing zinc-iron alloys on a substrate can include introducing a cathode and an anode into an electrolyte solution comprising an alkali metal citrate, an alkali metal acetate, a citric acid, and glycine. Electrodepositing can further include passing a current between the cathode and the anode through the electrolyte solution to deposit zinc and iron onto the cathode.

First claim

What is claimed is:

1. A method for electrodepositing a zinc-iron alloy on a substrate, the method comprising:
introducing a cathode and an anode into an electrolyte solution comprising a zinc salt, an iron salt, an alkali metal citrate, an alkali metal acetate, a citric acid, and glycine, the electrolyte solution having a glycine concentration from about 0.1 moles per liter (mol/L) to about 2 mol/L and an alkali metal citrate concentration from about 0.001 mol/L to about 0.1 mol/L; and
passing a first current between the cathode and the anode through the electrolyte solution to deposit a first layer containing zinc and iron onto the cathode, the first current having a first current density from about 1 mA/cm 2 to about 500 mA/cm 2 .

2. The method of claim 1 , wherein the electrolyte solution further comprises thiamine hydrochloride.

3. The method of claim 2 , wherein the electrolyte solution comprises a concentration of the thiamine hydrochloride from about 0.0001 moles per liter (mol/L) to about 1 mol/L.

4. The method of claim 3 , wherein a concentration of the thiamine hydrochloride in the electrolyte solution is about 0.0015 mol/L.

5. The method of claim 1 , wherein the cathode is a steel substrate, a copper substrate, a brass substrate, a nickel substrate, a copper-coated substrate, or a nickel-coated substrate.

6. The method of claim 1 , wherein the anode is a zinc material, platinum material, platinized titanium material, or a carbonaceous electrode material.

7. The method of claim 1 , wherein the first current has a first current density from about 5 mA/cm 2 to about 200 mA/cm 2 .

8. The method of claim 7 , wherein the first current includes a pulsed current formed from a series of pulses and each pulse has a duration of from about 20 milliseconds to about 800 milliseconds.

9. The method of claim 8 , wherein a temperature of the electrolyte solution is maintained at a temperature from about 20° C. to about 35° C. while passing the first current.

10. The method of claim 1 , further comprising passing a second current between the cathode and the anode to deposit a second layer comprising zinc and iron onto the first layer, the second current having a second current density from about 5 mA/cm 2 to about 500 mA/cm 2 , the second current density being different than the first current density.

11. The method of claim 10 , further comprising repeating passing the first current and the second current between the cathode and the anode to form a coating having a plurality of alternating layers, wherein the plurality of alternating layers have substantially the same thickness and two or more of the layers have a different iron content.

12. The method of claim 10 , further comprising repeating passing the first current and the second current between the cathode and the anode to form a coating having a plurality of alternating layers, wherein two or more of the plurality of alternating layers have a different thickness and two or more of the plurality of alternating layers have a different iron content.

13. The method of claim 10 , further comprising repeating passing the first current and the second current between the cathode and the anode to form a coating having a plurality of alternating layers comprising:
the first layer having a first iron content,
the second layer having a second iron content different than the first iron content,
a third layer having the same iron content as the first layer, and
a fourth layer having the same iron content as the second layer.

14. The method of claim 10 , further comprising repeating passing the first current and the second current between the cathode and the anode to form a coating having a plurality of alternating layers, wherein each layer has substantially the same thickness and each layer has a different iron content.

15. The method of claim 10 , further comprising repeating passing the first current and the second current between the cathode and the anode to form a coating having a plurality of alternating layers, wherein each layer has a different thickness and each layer has a different iron content.

16. The method of claim 1 , further comprising passing a second current between the cathode and the anode having the same current density as the first current density of the first current to deposit a second layer comprising zinc and iron onto the first layer deposited by the first current.

17. The method of claim 16 , further comprising repeating passing the first current and the second current between the cathode and the anode to form a coating having a plurality of alternating layers having an iron content, wherein each of the first current and the second current substantially the same duration and the plurality of alternating layers have substantially the same thickness and substantially the same iron content.

18. The method of claim 1 , wherein first layer comprises an iron content from about 8.9 wt. % to about 62.4 wt. %.

19. The method of claim 1 , wherein a concentration of the alkali metal citrate in the electrolyte solution is about 0.018 mol/L.

20. The method of claim 1 , wherein a concentration of the glycine in the electrolyte solution is about 0.146 mol/L.

21. A method for electrodepositing a zinc-iron alloy on a substrate, the method comprising:
introducing a cathode and an anode into an electrolyte solution comprising a zinc salt, an iron salt, an alkali metal citrate, an alkali metal acetate, a citric acid, thiamine hydrochloride, and glycine, the electrolyte solution having a thiamine hydrochloride concentration from about 0.0001 moles per liter (mol/L) to about 1 mol/L an alkali metal citrate concentration from about 0.001 mol/L to about 0.1 mol/L, have been inserted after the concentration “1 mol/L”, and a glycine concentration from about 0.1 mol/L to about 2 mol/L;
passing a first current having a first current density between the cathode and the anode through the electrolyte solution to deposit a first layer containing zinc and iron onto the cathode to form a zinc-iron alloy on a substrate, the first layer comprising an iron content from about 8.9 wt. % to about 62.4 wt. %; and
passing a second current between the cathode and the anode to deposit a second layer comprising zinc and iron onto the first layer, the second current having a second current density, wherein each of the first current density and the second current density is from about 1 mA/cm 2 to about 500 mA/cm 2 , the first current density being different than the second current density.

22. The method of claim 21 , wherein a concentration of the thiamine hydrochloride in the electrolyte solution is about 0.0015 mol/L.

23. The method of claim 21 , wherein a concentration of the glycine in the electrolyte solution is about 0.146 mol/L.

24. A method for electrodepositing a zinc-iron alloy on a substrate, the method comprising:
introducing a cathode and an anode into an electrolyte solution comprising a zinc salt, an iron salt, an alkali metal citrate, an alkali metal acetate, a citric acid, and glycine, the electrolyte solution having a glycine concentration from about 0.1 mol/L to about 2 mol/L and an alkali metal citrate concentration from about 0.001 mol/L to about 0.1 mol/L have been inserted after the concentration “mol/L”;
passing a first current having a first current density between the cathode and the anode through the electrolyte solution to deposit a first layer containing zinc and iron onto the cathode

Assignees

• Boeing Co

Inventors

• Gaydos Stephen P
• Ijeri Vijaykumar S
• Prakash Om
• Mishra Trilochan
• Singh Raghuvir
• Tiwari Shashi Kant

Classifications

• C25D3/24 Primary

  from cyanide baths · CPC title

• C25D5/627

  Electroplating characterised by the visual appearance of the layers, e.g. colour, brightness or mat appearance · CPC title

• C25D5/623

  Porosity of the layers · CPC title

• C25D3/562 Primary

  containing more than 50% by weight of iron or nickel or cobalt · CPC title

• C25D5/18 Primary

  Electroplating using modulated, pulsed or reversing current · CPC title