System and method for parallel solution extraction of one or more metal values from metal-bearing materials
US-2015361527-A1 · Dec 17, 2015 · US
US9637806B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9637806-B2 |
| Application number | US-201314424254-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 29, 2013 |
| Priority date | Aug 31, 2012 |
| Publication date | May 2, 2017 |
| Grant date | May 2, 2017 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Described herein are methods of recovering silver from solution to produce metallic (i.e., elemental) silver. These methods generally include a step of providing a silver-containing aqueous solution that includes cationic silver species, followed by a step of forming a reaction solution that includes an organic acid, a buffering agent, and the cationic silver species, and a step of generating a reaction product that includes metallic silver by reducing the concentration of the cationic silver species in the reaction solution. Also described herein are metallic or elemental silver produced by these methods.
Opening claim text (preview).
What is claimed is: 1. A method for treating a silver-containing solution, the method comprising: providing a silver-containing aqueous solution comprising cationic silver species; disposing an organic acid and a buffering agent in the silver-containing aqueous solution to form a reaction solution comprising a concentration of the organic acid, a concentration of the buffering agent, and a concentration of the cationic silver species, wherein the concentration of the organic acid is equimolar to or in a stoichiometric excess of the concentration of the cationic silver species, and wherein the buffering agent comprises citric acid and at least one of sodium phosphate dibasic and sodium phosphate monobasic; and generating a reaction product comprising metallic silver, thereby reducing the concentration of the cationic silver species in the reaction solution, wherein the metallic silver is precipitated from the solution. 2. The method of claim 1 , wherein the silver-containing aqueous solution comprises silver nitrate, silver nitrite, silver sulfate, silver phosphate, a silver halide, or a mixture thereof. 3. The method of claim 1 , wherein the organic acid comprises lactic acid, citric acid, oxalic acid, ascorbic acid, fumaric acid, maleic acid, or a mixture thereof. 4. The method of claim 1 , wherein the generating comprises heating the reaction solution and/or mixing the reaction solution. 5. The method of claim 4 , wherein the temperature of the heating is less than, or equal to about 90 degrees Celsius. 6. The method of claim 1 , wherein a duration of the generating is about 5 minutes to about 24 hours. 7. The method of claim 1 , further comprising adjusting an initial pH of the reaction solution before generating the reaction product. 8. The method of claim 1 , further comprising recovering the metallic silver. 9. The method of claim 8 , wherein the recovering comprises separating the metallic silver from a remaining portion of the reaction product and the reaction solution. 10. The method of claim 8 , wherein the reduced concentration of the cationic silver species in the reaction solution is less than or equal to about 5 parts per million. 11. The method of claim 1 , wherein the metallic silver is produced in a fractional yield of greater than 90 percent. 12. The method of claim 1 , wherein the metallic silver has an average particle size of about 120 nm to about 400 nm. 13. The method of claim 1 , wherein the metallic silver comprises less than 20 parts per million of non-silver metals. 14. A method for treating a silver-containing solution, the method comprising: providing a silver-containing aqueous solution comprising cationic silver species; disposing ascorbic acid and a buffering agent comprising sodium phosphate dibasic and citric acid in the silver-containing aqueous solution to form a reaction solution comprising a concentration of the ascorbic acid, a concentration of the buffering agent, and a concentration of the cationic silver species, wherein the concentration of the ascorbic acid is equimolar to or in a stoichiometric excess of the concentration of the cationic silver species; generating a reaction product comprising metallic silver, thereby reducing the concentration of the cationic silver species in the reaction solution to less than or equal to about 5 parts per million, wherein the metallic silver is precipitated from the solution; and separating the metallic silver from a remaining portion of the reaction product and the reaction solution by decanting. 15. The method of claim 14 , further comprising adjusting an pH of the reaction solution before generating the reaction product to a pH about 6 to about 7. 16. The method of claim 14 , wherein the metallic silver comprises less than 20 parts per million of non-silver metals and has an average particle size of about 120 nm to about 400 nm. 17. A method for treating a silver-containing solution, the method comprising: providing a silver-containing aqueous solution comprising cationic silver species; disposing an organic acid and a buffering agent formed from a combination of sodium phosphate dibasic and citric acid in the silver-containing aqueous solution to form a reaction solution comprising a concentration of the organic acid, a concentration of the buffering agent, and a concentration of the cationic silver species, wherein the concentration of the organic acid is equimolar to or in a stoichiometric excess of the concentration of the cationic silver species; generating a reaction product comprising metallic silver, thereby reducing the concentration of the cationic silver species in the reaction solution to less than or equal to about 5 parts per million, wherein the metallic silver has an average particle size of about 120 nm to about 400 nm and is precipitated from the solution; and separating the metallic silver from a remaining portion of the reaction product and the reaction solution by decanting, wherein the buffering agent is capable of maintaining a stable pH of about 6 to about 7 during the generating a reaction product step.
Submicron particles having a size above 100 nm up to 300 nm · CPC title
Nanotechnology for materials or surface science, e.g. nanocomposites · CPC title
Heavy metals or heavy metal compounds · CPC title
Operations & Transport · mapped topic
using specific organic precipitants · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.