Regeneration of cupric etchants and recovery of copper sulfate
View Patent ↗Spent, acidic solutions comprising cupric chloride and hyrdrochloric acid from the copper etching process are regenerated by a process in which the acid is subjected to distillation with sulfuric acid. In one embodiment, the process comprises (a) providing a spent etchant comprising at least about 10% by weight chloride and at least about 5% dissolved copper; (b) adding at least about 2 moles of sulfuric acid per mole of dissolved copper to the spent etching solution, thereby converting copper chloride into hydrochloric acid and precipitated copper sulfate; (c) distilling the mixture from step (b) to vaporize at least a portion of the hydrochloric acid; (d) condensing at least a portion of the vaporized hydrochloric acid; (e) separating at least a portion of the precipitated copper sulfate from the residual liquid, wherein said residual liquid comprises sulfuric acid; and (f) reusing at least a portion of the residual liquid as a sulfuric acid source in step (b).
1. A process for the regeneration of a spent etching solution comprising dissolved copper chloride, the process comprising the steps of:
(a) providing a spent etchant comprising at least about 10% by weight chloride and at least about 5% dissolved copper;
(b) adding at least about 2 moles of sulfuric acid per mole of dissolved copper to the spent etching solution, thereby converting copper chloride into hydrochloric acid and precipitated copper sulfate;
(c) distilling the mixture from step (b) to vaporize at least a portion of the hydrochloric acid;
(d) condensing at least a portion of the vaporized hydrochloric acid;
(e) separating at least a portion of the precipitated copper sulfate from the residual liquid, wherein said residual liquid comprises sulfuric acid; and
(f) reusing at least a portion of the residual liquid as a sulfuric acid source in step (b).
2. The process of claim 1 , wherein the process operates on a continuous basis, and wherein the spent etchant, the sulfuric acid, or both further comprise at least one mole of water per mole of dissolved copper in the spent etchant.
3. The process of claim 1 , wherein the process operates on a batch basis, and wherein the spent etchant, the sulfuric acid, or both further comprise at least one mole of water per mole of dissolved copper in the spent etchant.
4. The process of claim 1 , wherein the quantity of sulfuric acid added is at least about 3 moles of sulfuric acid per mole of dissolved copper in the spent etchant.
5. The process of claim 1 , wherein the quantity of sulfuric acid added is at least about 3.5 moles of sulfuric acid per mole of dissolved copper in the spent etchant.
6. The process of claim 1 , wherein the quantity of sulfuric acid added is between about 4 moles and about 6 moles sulfuric acid per mole dissolved copper in the spent etchant.
7. The process of claim 1 , wherein the quantity of sulfuric acid added is between about 3.5 moles and about 5 moles sulfuric acid per mole dissolved copper in the spent etchant.
8. The process of claim 1 , wherein at least 4 parts by weight of sulfuric acid added per 6 parts by weight of spent etchant.
9. The process of claim 1 , wherein at least 5 parts by weight of sulfuric acid added per 5 parts by weight of spent etchant.
10. The process of claim 1 , wherein at least 6 parts by weight of sulfuric acid added per 4 parts by weight of spent etchant.
11. The process of claim 1 , wherein the distillation in step (c) occurs at a temperature of from about 95° C. to about 135° C.
12. The process of claim 1 , wherein the distillation in step (c) occurs at a temperature of from about 120° C. to about 135° C.
13. The process of claim 1 , wherein the distillation in step (c) occurs at a pressure of less than about 1 atm.
14. The process of claim 13 , wherein the distillation in step (c) occurs at a pressure of from about 0.7 to about 0.99 atm.
15. The process of claim 1 , wherein the separated copper sulfate comprises residual liquid, the process further comprising contacting the separated copper sulfate with a base to neutralize at least a portion of the sulfuric acid in the residual liquid contacting the separated copper sulfate.
16. The process of claim 1 , wherein the precipitated copper sulfate is separated from the residual liquid comprising sulfuric acid by centrifugation.
17. The process of claim 1 , wherein the recovered hydrochloric acid comprises at least about 8 moles hydrochloric acid per liter, further comprising the step of formulating at least a portion of the condensed hydrochloric acid into a copper etchant.
18. The process of claim 1 , wherein the spent etching solution in step (a) comprises from about 4 to about 8 moles per liter total chloride.
19. The process of claim 1 , wherein step (a) further comprises concentrating the spent etchant to at least about 20 weight % chloride.
20. The process of claim 1 , wherein step (a) further comprises concentrating a spent etching solution to provide a spent etchant comprising at least about 30 weight % chloride.
21. The process of claim 1 , wherein the separated copper sulfate comprises at least about 90% by weight of copper sulfate pentahydrate and/or copper sulfate monohydrate.
22. The process of claim 21 , wherein more than 60 mole percent of the separated copper sulfate comprises copper sulfate pentahydrate.
23. The process of claim 21 , wherein more than 60 mole percent of the separated copper sulfate comprises copper sulfate monohydrate.
24. The process of claim 21 , wherein more than 80 mole percent of the separated copper sulfate comprises copper sulfate monohydrate.
25. The process of claim 1 , further comprising the step of converting at least a portion of the separated copper sulfate into a form where wherein the copper can be injected into wood, and injecting the copper into wood as a wood preservative.
26. The process of claim 1 , further comprising the step of converting at least a portion of the separated copper sulfate into a fungicidal composition.
27. The process of claim 1 , further comprising the step of washing the separated copper sulfate to further remove residual liquid.
28. The process of claim 1 , wherein the composition comprising reaction products of the spent etchant and sulfuric acid is steam distilled to vaporize more than 98% of the chloride in the composition as hydrochloric acid.
29. The process of claim 1 , wherein at least about 90 weight % of the Cu in the spent etchant is recovered as separated copper sulfate.