System and Method for Recovering Catalytic Precious Metal from Aqueous Galvanic Processing Solution
US-2018245178-A1 · Aug 30, 2018 · US
US9834825B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9834825-B2 |
| Application number | US-201514695496-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 24, 2015 |
| Priority date | Sep 12, 2014 |
| Publication date | Dec 5, 2017 |
| Grant date | Dec 5, 2017 |
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A method for collecting silver ions and phosphoric acid in a waste fluid includes collecting silver chloride from the waste fluid, collecting silver chloride including providing a chloride compound to the waste fluid; and collecting phosphoric acid, collecting phosphoric acid including distilling the waste fluid from which the silver chloride has been collected.
Opening claim text (preview).
What is claimed is: 1. A method for collecting silver ions and phosphoric acid in a waste fluid, the method comprising: collecting silver chloride from the waste fluid by adding a chloride compound to the waste fluid; and collecting phosphoric acid by distilling the waste fluid from which the silver chloride has been collected. 2. The method as claimed in claim 1 , wherein the chloride compound includes at least one of HCl, NaCl, CaCl 2 , or KCl. 3. The method as claimed in claim 1 , wherein collecting silver chloride from the waste fluid includes: generating a mixed waste fluid by adding the chloride compound to the waste fluid; and separating the silver chloride by filtering the mixed waste fluid. 4. The method as claimed in claim 3 , wherein separating the silver chloride is performed by using at least one of vacuum filtration, pressure filtration, or gravity filtration. 5. The method as claimed in claim 3 , wherein generating the mixed waste fluid is performed at a temperature of about 25° C. to about 80° C. 6. The method as claimed in claim 3 , wherein generating the mixed waste fluid is performed for about 10 minutes to about 120 minutes. 7. The method as claimed in claim 1 , wherein: the waste fluid includes silver ions, and a molar ratio between the chloride compound and the silver ions is about 1:2 to about 1:3. 8. The method as claimed in claim 1 , further comprising obtaining silver metal from the collected silver chloride. 9. The method as claimed in claim 8 , wherein obtaining silver metal is performed by using at least one of electrolysis, pyrolysis, or chemical treatment. 10. The method as claimed in claim 1 , wherein the chloride compound is an aqueous solution or a solid powder. 11. The method as claimed in claim 1 , wherein collecting phosphoric acid is performed at a temperature of about 80° C. to about 150° C. 12. The method as claimed in claim 1 , wherein collecting phosphoric acid is performed under a pressure of about 1 mmHg to about 760 mmHg. 13. A method for collecting silver ions and phosphoric acid in a waste fluid, the method comprising: generating an acidic aqueous solution by distilling the waste fluid to remove volatile impurities from the waste fluid; adding a chloride compound to the acidic aqueous solution; and collecting silver chloride and phosphoric acid from the acidic aqueous solution to which the chloride compound has been added. 14. The method as claimed in claim 13 , wherein collecting silver chloride and phosphoric acid includes: collecting precipitated silver chloride by filtering the acidic aqueous solution to provide a filtered acidic aqueous solution; and collecting the phosphoric acid from the filtered acidic aqueous solution. 15. The method as claimed in claim 13 , wherein generating the acidic aqueous solution is performed at a temperature of about 80° C. to about 150° C. 16. The method as claimed in claim 13 , wherein generating the acidic aqueous solution is performed under a pressure of about 1 mmHg to about 760 mmHg. 17. The method as claimed in claim 13 , wherein the chloride compound includes one or more of HCl, NaCl, CaCl 2 , or KCl. 18. The method as claimed in claim 13 , wherein the chloride compound is an aqueous solution or a solid powder. 19. The method as claimed in claim 13 , wherein collecting silver chloride and phosphoric acid is performed at a temperature of about 25° C. to about 80° C. 20. The method as claimed in claim 13 , wherein collecting silver chloride and phosphoric acid is performed for about 10 minutes to about 120 minutes.
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