Acid mist suppression in copper electrowinning
US-12098474-B2 · Sep 24, 2024 · US
US10597790B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10597790-B2 |
| Application number | US-201615194366-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 27, 2016 |
| Priority date | May 10, 2016 |
| Publication date | Mar 24, 2020 |
| Grant date | Mar 24, 2020 |
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A method of producing a refined copper includes depositing the refined copper on a cathode by an electroplating process or an electroless plating process in an alkaline plating bath including a solution of a copper compound that includes none of sulfur, chlorine and oxygen elements and produces copper ions having a valence of +1 in the solution.
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What is claimed is: 1. A method of producing a refined copper, the method comprising: manufacturing a copper plate of not less than 3 mm in thickness by depositing the refined copper on a cathode by an electroplating process or an electroless plating process in an alkaline plating bath comprising a solution of a copper compound consisting of a copper cyanide that does not include any of sulfur, chlorine, and oxygen elements, and produces copper ions having a valence of +1 in the solution, wherein a sulfur concentration in an entirety of the copper plate is not more than 3.1 mass ppm, a chlorine concentration in the entirety of the copper plate is not more than 1.1 mass ppm, a sulfur concentration in the copper plate from an outermost surface to a depth of 80 nm is not less than 200 mass ppm and not more than 620 mass ppm, and chlorine concentration in the copper plate from the outermost surface to a depth of 60 nm is not less than 400 mass ppm and not more than 700 mass ppm. 2. The method according to claim 1 , wherein a sulfur concentration in the refined copper from the outermost surface to a depth of 2.5 is not more than 300 mass ppm. 3. The method according to claim 1 , wherein the chlorine concentration in the refined copper from the outermost surface to a depth of 2.5 μm is not more than 61 mass ppm. 4. The method according to claim 1 , wherein a particle size on a surface of the refined copper is not less than 0.5 μm and not more than 5 μm. 5. The method according to claim 1 , wherein a starting sheet comprising copper is used as the cathode and is included in the refined copper, and wherein a sulfur concentration in an entirety of the refined copper including the starting sheet is not more than 3.1 mass ppm. 6. The method according to claim 1 , wherein a starting sheet comprising copper is used as the cathode and is included in the refined copper, and wherein a chlorine concentration in an entirety of the relined copper including the starting sheet is not more than 1.1 mass ppm. 7. The method according to claim 1 , wherein a conductive metal plate comprising an alloy including at least one of stainless steel, transition metals, or transition metal elements is used as the cathode, and wherein the refined copper is obtained by stripping from the conductive metal plate. 8. The method according to claim 1 , wherein a conductive plate comprising a composite material comprising a metal in a form of a mesh or a plate, and a carbon nanotube is used as the cathode, and wherein the refined copper is obtained by stripping from the conductive plate. 9. The method according to claim 1 , wherein the depositing the refined copper on the cathode is performed by the electroless plating process. 10. The method according to claim 1 , wherein the thickness of the copper plate is in a range from 4 mm to 10 mm. 11. The method according to claim 1 , wherein the sulfur concentration in the entirety of the copper plate is not more than 3 mass ppm. 12. The method according to claim 11 , wherein the chlorine concentration in the entirety of the copper plate is not more than 1 mass ppm. 13. The method according to claim 1 , wherein the chlorine concentration in the entirety of the copper plate is not more than 1 mass ppm.
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