Flotation reagents and flotation processes utilizing same
US-10130956-B2 · Nov 20, 2018 · US
US2022119913A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2022119913-A1 |
| Application number | US-202117496329-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 7, 2021 |
| Priority date | Oct 16, 2020 |
| Publication date | Apr 21, 2022 |
| Grant date | — |
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The present disclosure provides a method of recovering copper, molybdenum, and a precious metal value from a metal-bearing material, the method comprising bulk flotation of the metal-bearing material to form a flotation product, wherein the metal-bearing material comprises a copper compound, a molybdenum compound, and at least one precious metal value, pressure oxidizing the flotation product to form a pressure oxidized discharge, separating the pressure oxidized discharge to form a separated liquid and separated solid, extracting molybdenum, via a molybdenum solution extraction, from the separated liquid to form a molybdenum-containing stream and a copper-containing stream, extracting copper, via a copper solution extraction, from the copper-containing stream, and extracting the precious metal value, via a cyanide leaching process, from the separated solid.
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What is claimed is: 1 . A method of recovering copper, molybdenum, and a precious metal value from a metal-bearing material, the method comprising: bulk flotation of the metal-bearing material to form a flotation product, wherein the metal-bearing material comprises a copper compound, a molybdenum compound, and at least one precious metal value; pressure oxidizing the flotation product to form a pressure oxidized discharge; separating the pressure oxidized discharge to form a separated liquid and separated solid; extracting molybdenum, via a molybdenum solution extraction, from the separated liquid to form a molybdenum-containing stream and a copper-containing stream; extracting copper, via a copper solution extraction, from the copper-containing stream; and extracting the precious metal value, via a cyanide leaching process, from the separated solid. 2 . The method of claim 1 , further comprising conducting an organic washing process on the molybdenum-containing stream and conducting an organic stripping process on the molybdenum-containing stream. 3 . The method of claim 2 , further comprising conducting a crystallization process on the molybdenum containing stream. 4 . The method of claim 1 , wherein extracting the precious metal value from the separated solid further comprises a hot lime boil. 5 . The method of claim 1 , wherein extracting copper from the copper-containing stream further comprises electrowinning the copper-containing stream. 6 . The method of claim 1 , further comprising cooling the pressure oxidized discharge via flash letdown process. 7 . A method of recovering copper, molybdenum, and a precious metal value from a metal-bearing material, the method comprising: bulk flotation of the metal-bearing material to form a flotation product, wherein the metal-bearing material comprises a copper compound, a molybdenum compound, and at least one precious metal value; pressure oxidizing the flotation product to form a pressure oxidized discharge; separating the pressure oxidized discharge to form a separated liquid and separated solid; extracting molybdenum, via a molybdenum solution extraction, from the separated liquid to form a molybdenum-containing stream and a copper-containing stream; extracting copper, via a copper solution extraction, from the copper-containing stream; and extracting the precious metal value, via a thiosulfate leaching process, from the separated solid. 8 . The method of claim 7 , further comprising conducting an organic washing process on the molybdenum-containing stream and conducting an organic stripping process on the molybdenum-containing stream. 9 . The method of claim 8 , further comprising conducting a crystallization process on the molybdenum containing stream. 10 . The method of claim 7 , wherein extracting the precious metal value from the separated solid further comprises a hot lime boil. 11 . The method of claim 7 , wherein extracting copper from the copper-containing stream further comprises electrowinning the copper-containing stream. 12 . The method of claim 7 , further comprising cooling the pressure oxidized discharge via flash letdown process. 13 . A method of recovering copper, molybdenum, and a precious metal value from a metal-bearing material, the method comprising: bulk flotation of the metal-bearing material to form a flotation product, wherein the metal-bearing material comprises a copper compound, a molybdenum compound, and at least one precious metal value; pressure oxidizing the flotation product to form a pressure oxidized discharge; hot curing the pressure oxidized discharge to form a product stream; separating the pressure oxidized discharge to form a separated liquid and separated solid; extracting molybdenum, via a molybdenum solution extraction, from the separated liquid to form a molybdenum-containing stream and a copper-containing stream; extracting copper, via a copper solution extraction, from the copper-containing stream; and extracting the precious metal value from the separated solid. 14 . The method of claim 13 , further comprising conducting an organic washing process on the molybdenum-containing stream and conducting an organic stripping process on the molybdenum-containing stream. 15 . The method of claim 14 , further comprising conducting a crystallization process on the molybdenum containing stream. 16 . The method of claim 13 , wherein extracting the precious metal value from the separated solid further comprises a cyanide leaching process. 17 . The method of claim 13 , wherein extracting the precious metal value from the separated solid further comprises a thiosulfate leaching process. 18 . The method of claim 13 , wherein extracting the precious metal value from the separated solid further comprises a hot lime boil and a cyanide leaching process. 19 . The method of claim 18 , wherein the lime boil utilizes a temperature of between approximately 0° C. and approximately 180° C. for a duration of between approximately 0 to 6 hours. 20 . The method of claim 13 , wherein the hot curing comprises holding the pressure oxidized discharge at a temperature of between approximately 0 and 180° C. for a duration between approximately 4 to 12 hours.
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