Method for the recovery of metals from electronic waste
US-12571069-B2 · Mar 10, 2026 · US
US10435769B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10435769-B2 |
| Application number | US-201916247900-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 15, 2019 |
| Priority date | Jul 22, 2016 |
| Publication date | Oct 8, 2019 |
| Grant date | Oct 8, 2019 |
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.
A method for refining sulfidic copper concentrate includes feeding sulfidic copper concentrate and oxygen-bearing reaction gas and slag forming material into a reaction shaft of a suspension smelting furnace, collecting slag and blister copper in a settler of the suspension smelting furnace to form a blister layer containing blister copper and a slag layer, and discharging slag and blister copper separately from the settler of the suspension smelting furnace, so that slag is fed into an electric furnace. The method further includes feeding a part of the sulfidic copper concentrate into the electric furnace.
Opening claim text (preview).
The invention claimed is: 1. A method for refining sulfidic copper concentrate, the method comprising: feeding a first portion of sulfidic copper concentrate and oxygen-bearing reaction gas and slag forming material into a reaction shaft of a suspension smelting furnace by means of a burner that is arranged on top of the reaction shaft of the suspension smelting furnace, whereby sulfidic copper concentrate and oxygen-bearing reaction gas and slag forming material react in the reaction shaft of the suspension smelting furnace into blister copper and slag; collecting slag and blister copper in a settler of the suspension smelting furnace to form a blister layer containing blister copper and a slag layer containing slag on top of the blister layer; discharging slag in an unreduced state and blister copper separately from the settler of the suspension smelting furnace, so that slag in an unreduced state is fed into an electric furnace; feeding a second portion of sulfidic copper concentrate into the electric furnace; reducing the slag that is fed in the unreduced state from the suspension smelting furnace in the electric furnace at least partly with the second portion of sulfidic copper concentrate that is fed into the electric furnace to form a matte layer containing copper matte and an electric furnace slag layer containing electric furnace slag on top of the matte layer; discharging electric furnace slag and matte copper separately from the electric furnace; granulating and treating the copper matte that is discharged from the electric furnace to obtain copper matte feed material; and feeding at least a part of the copper matte feed material into the reaction shaft of the suspension smelting furnace by means of the burner. 2. The method according to claim 1 , further comprising: feeding blister copper from the settler of the suspension smelting furnace into an anode furnace; fire refining the blister copper in the anode furnace. 3. The method according to claim 1 , further comprising: subjecting the electric furnace slag to a final slag treatment process to form reject and slag concentrate or other copper containing product; and feeding the slag concentrate or other copper containing product by means of the burner into the reaction shaft of the suspension smelting furnace. 4. The method according to claim 1 , further comprising: feeding a carbon containing reducing agent into the electric furnace, wherein the carbon containing reducing agent is coke. 5. The method according to claim 1 , further comprising: feeding process gases from an uptake of the suspension smelting furnace to a process gas treatment arrangement. 6. The method according to claim 1 , further comprising: feeding process gases from the electric furnace to a process gas treatment arrangement. 7. The method according to claim 1 , wherein the second portion of sulfidic copper concentrate that is fed into the electric furnace includes between 5 and 50% of the total amount of sulfidic copper concentrate, the total amount of sulfidic copper concentrate comprising the first and second portions of sulfidic copper concentrate. 8. The method according to claim 1 , wherein the second portion of sulfidic copper concentrate that is fed into the electric furnace includes between 10 and 40% of the total amount of sulfidic copper concentrate, the total amount of sulfidic copper concentrate comprising the first and second portions of sulfidic copper concentrate. 9. The method according to claim 1 , wherein the second portion of sulfidic copper concentrate that is fed into the electric furnace includes between 25 and 35% of the total amount of sulfidic copper concentrate, the total amount of sulfidic copper concentrate comprising the first and second portions of sulfidic copper concentrate. 10. The method according to claim 1 , wherein the mass ratio of the second portion of the sulfidic copper concentrate that is fed into the electric furnace to slag that is fed into the electric furnace is smaller than 1 to 1. 11. The method according to claim 10 , wherein the mass ratio of the second portion of the sulfidic copper concentrate that is fed into the electric furnace to slag that is fed into the electric furnace is between 0.25 to 1 and 0.7 to 1. 12. The method according to claim 10 , wherein the mass ratio of the second portion of the sulfidic copper concentrate that is fed into the electric furnace to slag that is fed into the electric furnace is between 0.25 to 1 and 0.7 to 1. 13. The method according to claim 1 , wherein the moisture content of the second portion of the sulfidic copper concentrate that is fed into the electric furnace is below 1% by weight. 14. The method according to claim 1 , wherein the moisture content of the second portion of the sulfidic copper concentrate that is fed into the electric furnace is below 0.5% by weight. 15. The method according to claim 1 , wherein the moisture content of the first portion of the sulfidic copper concentrate that is fed into the reaction shaft of the suspension smelting furnace is below 1% by weight. 16. The method according to claim 1 , wherein the moisture content of the first portion of the sulfidic copper concentrate that is fed into the reaction shaft of the suspension smelting furnace is below 0.5% by weight. 17. The method according to claim 1 , wherein the second portion of the sulfidic copper concentrate that is fed into the electric furnace includes about 33% of the total amount of sulfidic copper concentrate, the total amount of sulfidic copper concentrate comprising the first and second portions of sulfidic copper concentrate.
by sulfides; Roasting reaction methods · CPC title
Reduction smelting or converting · CPC title
flash smelting or converting · CPC title
Slag, slime, speiss, or dross treating · CPC title
Smelting or converting · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.