Methods, systems and apparatuses for copper removal from aluminum desmutting solutions

Patent metadata

Field	Value
Publication number	US-10745812-B2
Application number	US-201715685263-A
Country	US
Kind code	B2
Filing date	Aug 24, 2017
Priority date	Aug 24, 2017
Publication date	Aug 18, 2020
Grant date	Aug 18, 2020

Abstract

Methods, systems and apparatuses are disclosed for treating aluminum desmutting solutions by reacting, mixing and filtering an aluminum desmutting solution flow from an aluminum desmutting solution tank and controlling the amount of copper ions in an aluminum desmutting solution tank by directing a portion of the desmutting solution from a desmutting solution tank to a treatment line, reacting a portion of the desmutting solution in the treatment line and recirculating a filtered aluminum desmutting solution to the aluminum desmutting solution tank during active desmutting operation of the aluminum desmutting solution tank.

First claim

What is claimed is:

1. A method of desmutting an aluminum workpiece comprising:
contacting the aluminum workpiece with an acidic aluminum desmutting solution, said acidic aluminum desmutting solution maintained at a pH ranging from about 1.0 to about 1.5;
directing at least a portion of an aluminum desmutting solution from an aluminum desmutting solution feed line directly to a mixing section during a substantially continuous operation of an aluminum desmutting process;
directing a flow of an aqueous reagent solution to the mixing section, said aqueous reagent solution comprising an iron cyanide compound;
contacting copper ions present in the portion of the acidic aluminum desmutting solution with the aqueous reagent solution to form a copper-containing precipitate in the mixing section;
filtering the copper-containing precipitate to form a filtered flow;
directing the filtered flow to a recirculating line via a filtered flow line;
forming a copper ion concentration in the filtered flow ranging from about 30 ppm to about 100 ppm; and
maintaining a copper concentration in the acidic aluminum desmutting solution at a copper concentration ranging from about 100 ppm copper to about 475 ppm during the substantially continuous operation of an aluminum desmutting process.

2. The method of claim 1 , wherein, in the step of directing at least a portion of the acidic aluminum desmutting solution, the portion of the aluminum desmutting solution comprises a flow rate ranging from about 1 gallons/min. to about 50 gallons/min.

3. The method of claim 1 , wherein, in the step of directing a flow of an aqueous reagent solution to the mixing section, the iron cyanide compound selected from the group consisting of: a ferricyanide; a ferrocyanide; a nitroprusside; and combinations thereof.

4. The method of claim 1 , wherein, in the step of directing a flow of an aqueous reagent solution to the mixing section, the iron cyanide compound is selected from the group consisting of: potassium ferricyanide; potassium ferrocyanide; sodium ferricyanide; sodium ferrocyanide; potassium nitroprusside; sodium nitroprusside; and combinations thereof.

5. The method of claim 1 , wherein, in the step of directing a flow of an aqueous reagent solution to the mixing section, the aqueous reagent solution concentration ranging from about 5% by weight to about 25% by weight.

6. The method of claim 1 , wherein in the step of directing a flow of an aqueous reagent solution to the mixing section, the reagent comprises potassium ferricyanide in a concentration of about 20% by weight.

7. The method of claim 1 , wherein in the step of contacting copper ions present in the acidic aluminum desmutting solution with the aqueous reagent solution to form a precipitate, the aqueous reagent solution is supplied to the aluminum desmutting solution at a mixing rate ranging from about 2 gallons per day to about 900 gallons per day of aqueous reagent combined with the aluminum desmutting solution.

8. The method of claim 1 , wherein the at least a portion of the aluminum desmutting solution is directed from the aluminum desmutting solution tank to the mixing section during substantially continuous active desmutting operation of the aluminum desmutting solution tank, and wherein the recirculating line returns the filtered flow to the aluminum desmutting solution tank during the substantially continuous active desmutting operation of the aluminum desmutting solution tank.

9. A method of treating an aluminum desmutting solution, the method comprising the steps of:
directing at least a portion of an aluminum desmutting solution from an aluminum desmutting solution tank to an aluminum desmutting solution feed line;
directing at least a diverted portion of the aluminum desmutting solution directly from the desmutting solution feed line to a mixing section, said aluminum desmutting solution maintained at a pH ranging from about 1.0 to about 1.5;
automatically directing an aqueous reagent solution from an aqueous reagent solution feed line to the mixing section when a copper ion concentration in the aluminum desmutting solution surpasses a predetermined concentration, said aqueous reagent solution comprising an iron cyanide compound;
contacting copper ions present in the aluminum desmutting solution with the aqueous reagent solution at the mixing section to form a precipitate, said precipitate comprising a copper-containing compound;
filtering the precipitate to form a first filtered flow; and
directing the first filtered flow to a recirculating line, said recirculating line in direct communication with the aluminum desmutting solution tank;
wherein the at least a portion of the aluminum desmutting solution is directed from the aluminum desmutting solution tank to the mixing section during substantially continuous active desmutting operation of the aluminum desmutting solution tank;
wherein the recirculating line returns the filtered flow to the aluminum desmutting solution tank during the substantially continuous active desmutting operation of the aluminum desmutting solution tank;
forming a treated aluminum desmutting solution in a desmutting bath; and
maintaining a copper concentration in the aluminum desmutting solution at a copper concentration ranging from about 100 ppm copper to about 475 ppm.

10. The method of claim 9 , wherein, in the step of directing at least a portion of the acidic aluminum desmutting solution, the portion of the acidic aluminum desmutting solution comprises a flow rate ranging from about 1 gallons/min. to about 50 gallons/min.

11. The method of claim 9 , wherein, in the step of directing an aqueous reagent solution, the iron cyanide compound selected from the group consisting of: a ferricyanide; a ferrocyanide; a nitroprusside; and combinations thereof.

12. The method of claim 9 , wherein, in the step of directing an aqueous reagent solution, the iron cyanide compound is selected from the group consisting of: potassium ferricyanide; potassium ferrocyanide; sodium ferricyanide; sodium ferrocyanide; potassium nitroprusside; sodium nitroprusside; and combinations thereof.

13. The method of claim 9 , wherein, in the step of directing an aqueous reagent solution comprises, the aqueous reagent solution concentration ranging from about 5% by weight to about 25% by weight.

14. The method of claim 9 , wherein in the step of directing an aqueous reagent solution comprises, the reagent comprises potassium ferricyanide in a concentration of about 20% by weight.

15. The method of claim 9 , wherein in the step of contacting copper ions present in the acidic aluminum desmutting solution with the aqueous reagent solution to form a precipitate, the aqueous reagent solution is supplied to the acidic aluminum desmutting solution at a mixing rate ranging from about 2 gallons per day to about 900 gallons per day.

16. The method of claim 9 , wherein, after the step of filtering the precipitate to form a filtered flow, further comprising:
directing the first filtered flow from a first filter outlet to a filter inlet of a second filter;
separating a further amount of precipitate in the second filter from the first filtered flow to form a second filtered flow; and
directing the second filtered flow from the second filter outlet to the recirculating line.

17. The method of claim 16 , wherein, in the step of separating a further amount of precipitate in the second filter, the second filtered flow comprising a copper ion concentration ranging from about 30 ppm to about 100 ppm.

18. The method of claim 9 , wh

Assignees

• Boeing Co

Inventors

• Crump David L
• Succo Lance E
• Huebner David
• Woodruff Mark R

Classifications

• B01D61/1471

  comprising multiple microfiltration steps · CPC title

• C23F1/46

  Regeneration of etching compositions · CPC title

• C23G3/00

  Apparatus for cleaning or pickling metallic material (with organic solvents C23G5/04) · CPC title

• C23G1/34

  Light metals · CPC title

• C23G1/103

  copper or alloys of copper · CPC title