Cyclone high-speed electrolyzer using high-speed turbulence, method for recovering valuable metals using the same, and valuable metals recovered therefrom
US-2025290214-A1 · Sep 18, 2025 · US
US9290827B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9290827-B2 |
| Application number | US-201213410975-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 2, 2012 |
| Priority date | Mar 4, 2011 |
| Publication date | Mar 22, 2016 |
| Grant date | Mar 22, 2016 |
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.
Disclosed is a method of leaching copper and gold from sulfide ores, which includes Process (1) of bringing a first aqueous acidic solution which contains chlorine ion, copper ion and iron ion, but no bromine ion, into contact with sulfide ores under supply of an oxidizing agent, so as to leach copper component contained in the sulfide ores; Process (2) of separating, by solid-liquid separation, a leaching reaction liquid obtained in Process (1), into a leaching residue and a leachate; and Process (3) of bringing a second aqueous acidic solution which contains chlorine ion, bromine ion, copper ion and iron ion, into contact with the leaching residue obtained in Process (2) under supply of an oxidizing agent, so as to leach gold contained in the leaching residue.
Opening claim text (preview).
What is claimed is: 1. A method of leaching copper and gold from sulfide ores, comprising: Process (1) of bringing a first aqueous acidic solution which contains chlorine ion, copper ion and iron ion, but no bromine ion, into contact with sulfide ores under supply of an oxidizing agent, so as to leach copper component contained in the sulfide ores; Process (2) of separating, by solid-liquid separation, a leaching reaction liquid obtained in Process (1), into a leaching residue and a leachate; and Process (3) of bringing a second aqueous acidic solution which contains chlorine ion, bromine ion, copper ion and iron ion, into contact with the leaching residue obtained in Process (2) under supply of an oxidizing agent, so as to leach gold contained in the leaching residue; wherein the redox potential (vs Ag/AgCl) of the first aqueous acidic solution at the start of Process (1) is 500 mV or above; wherein Process (1) terminates when conditions stating a copper leach rate of 90% by mass or more, and a gold leach rate of 10% by mass or less, are satisfied; wherein Process (1) terminates in the range of redox potential (vs Ag/AgCl) from 450 to 500 mV; and wherein the redox potential (vs Ag/AgCl) of the second aqueous acidic solution at the start of Process (2) is 550 mV or above. 2. The method according to claim 1 , wherein the concentration ratio by weight of bromine ion to chlorine ion in the second aqueous acidic solution is 1 or larger. 3. The method according to claim 1 , wherein the oxidizing agent used in Process (1) and Process (2) is air. 4. The method according to claim 1 , wherein the oxidizing agent used in Process (1) and Process (2) is air. 5. The method according to claim 2 , wherein the oxidizing agent used in Process (1) and Process (2) is air. 6. A method of leaching copper and gold from sulfide ores, comprising: Process (1) of bringing a first aqueous acidic solution which contains chlorine ion, copper ion and iron ion, but no bromine ion, into contact with sulfide ores under supply of an oxidizing agent, so as to leach copper component contained in the sulfide ores; Process (2) of separating, by solid-liquid separation, a leaching reaction liquid obtained in Process (1), into a leaching residue and a leachate; and Process (3) of bringing a second aqueous acidic solution which contains chlorine ion, bromine ion, copper ion and iron ion, into contact with the leaching residue obtained in Process (2) under supply of an oxidizing agent, so as to leach gold contained in the leaching residue, wherein Process (1) terminates in the range of redox potential (vs Ag/AgCl) from 450 to 500 mV; wherein the redox potential (vs Ag/AgCl) of the first aqueous acidic solution at the start of Process (1) is 500 mV or above; and wherein the redox potential (vs Ag/AgCl) of the second aqueous acidic solution at the start of Process (2) is 550 mV or above. 7. A method of leaching copper and gold from sulfide ores, comprising: Process (1) of bringing a first aqueous acidic solution which contains chlorine ion, copper ion and iron ion, but no bromine ion, into contact with sulfide ores under supply of an oxidizing agent, so as to leach copper component contained in the sulfide ores; Process (2) of separating, by solid-liquid separation, a leaching reaction liquid obtained in Process (1), into a leaching residue and a leachate; and Process (3) of bringing a second aqueous acidic solution which contains chlorine ion, bromine ion, copper ion and iron ion, into contact with the leaching residue obtained in Process (2) under supply of an oxidizing agent, so as to leach gold contained in the leaching residue, wherein Process (1) terminates when conditions reach a copper leach rate of 90% by mass or more, and a gold leach rate of 10% by mass or less, are satisfied; wherein the redox potential (vs Ag/AgCl) of the first aqueous acidic solution at the start of Process (1) is 500 mV or above; and wherein the redox potential (vs Ag/AgCl) of the second aqueous acidic solution at the start of Process (2) is 550 mV or above. 8. The method according to claim 1 , wherein the redox potential (vs Ag/AgCl) of the first aqueous acidic solution at the start of Process (1) is 550 mV or above. 9. The method according to claim 1 , wherein Process (1) terminates in the range of redox potential (vs Ag/AgCl) from 450 to 475 mV.
by wet processes (extraction of metal compounds by leaching in organic solutions C22B3/16; treatment or purification of solutions by liquid-liquid extraction C22B3/26) · CPC title
containing halogen · CPC title
in inorganic acid solutions {, e.g. with acids generated in situ; in inorganic salt solutions other than ammonium salt solutions} · CPC title
Cross-Sectional Technologies · mapped topic
Cross-Sectional Technologies · mapped topic
Related publications grouped by family.
Answers are generated from the same data shown on this page.