Process for reducing the amounts of zinc (zn) and lead (pb) in materials containing iron (fe)
US-2017058378-A1 · Mar 2, 2017 · US
US11519053B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11519053-B2 |
| Application number | US-201615572077-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 4, 2016 |
| Priority date | May 5, 2015 |
| Publication date | Dec 6, 2022 |
| Grant date | Dec 6, 2022 |
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.
The present invention provides a method for the treatment of sludge containing iron and between 4.5% to 12% by weight of zinc. This method includes a leaching step wherein leaching agents include hydrochloric acid and chlorate, and wherein the pH of the leachate directly resulting from this leaching step is set at a value below 1.5. A recycling method and treatment installation are also provided.
Opening claim text (preview).
The invention claimed is: 1. A method for the treatment of sludge, the method comprising the step of providing sludge, the sludge including iron and between 4.5% to 12% by weight of zinc; providing leaching agents, the leaching agents consisting of hydrochloric acid and chlorate; leaching the sludge with the leaching agents to form a leachate, a pH of leachate directly resulting from this leaching step being less than 1.5. 2. The method of claim 1 , wherein the leaching agents are provided in a solution. 3. The method of claim 2 , wherein the solution is a solution of hydrochloric acid and chlorates. 4. The method of claim 3 , wherein the chlorates are selected from the group consisting of an aqueous solution of NaClO 3 a powder of NaClO 3 , and a solution of KClO 3 . 5. The method according to claim 1 , wherein the leachate has a pH of at least 0.8. 6. A method for the treatment of sludge, the method comprising the step of providing sludge, the sludge including iron and between 4.5% to 12% by weight of zinc; providing leaching agents, the leaching agents consisting of hydrochloric acid and chlorate; leaching the sludge with the leaching agents to form a leachate, a pH of leachate directly resulting from this leaching step being greater than or equal to 0.8 and less than 1.5. 7. The method according to claim 6 , wherein the leachate has a pH between 0.8 and 1.2. 8. The method according to claim 6 , wherein the chlorate is a sodium chlorate compound. 9. The method according to claim 6 , wherein the leaching step is performed at a temperature between 50 and 65° C. 10. The method according to claim 6 , wherein the sludge initially contains 7%<Zn≤12%, by weight. 11. The method according to claim 6 , wherein the sludge initially contains between 1 and 2% by weight of lead. 12. The method according to claim 6 , further comprising: performing at least one separation step after the leaching step, in order to separate a leached sludge from a residual liquid in the leachate. 13. The method according to claim 12 , further comprising: performing an iron precipitation step after the at least one separation step to precipitate goethite. 14. The method according to claim 13 , further comprising: performing a zinc and lead precipitation step after the iron precipitation step to obtain zinc and lead hydroxides. 15. The method according to claim 13 , wherein the iron precipitation step includes lime addition. 16. The method according to claim 12 , further comprising: performing a single precipitation step after the at least one separation step to obtain a concentrate of zinc, lead and iron hydroxides. 17. The method according to claim 16 , wherein the single precipitation step includes lime addition. 18. The method according to claim 16 , wherein the zinc and lead precipitation step includes lime addition. 19. The method according to claim 6 , wherein the sludge has an initial composition comprising, with contents being expressed by weight: 15%<Fe<30%; 30%<C<60%; 1%<Pb≤2%; 2%<Al 2 O 3 <30%; 2%<CaO<5%; 0.5%<MgO<2%; 0.1%<Mn<0.2%; 0.05%<P<0.1%; 0.1%<TiO 2 ≤0.3%; 0.02%<Cr 2 O3<0.08%; 0.01%<ZrO 2 <0.05%; 0%<V 2 O 5 <0.03%; 0.05%<Ti≤0.2%; 22%<Fe2O3<38%; 0%<V≤0.007%; 4.5%<Zn<12%; and 1%<S<4%. 20. The method according to claim 6 , wherein the sludge is blast furnace sludge. 21. A recycling method comprising the steps of: treating blast furnace sludge with the method according to claim 6 ; and sending the treated blast furnace sludge to a sintering plant. 22. A method for the treatment of sludge, the method comprising the step of providing sludge, the sludge including iron and between 4.5% to 12% by weight of zinc; providing leaching agents, the leaching agents consisting of hydrochloric acid and chlorate; leaching the sludge with the leaching agents to form a leachate, a pH of leachate directly resulting from this leaching step being greater than or equal to 0.8 and less than 1.5, wherein a final product is a sludge containing less than 0.40% by weight in zinc and less than 0.10% by weight in lead.
Obtaining lead · CPC title
in inorganic acid solutions {, e.g. with acids generated in situ; in inorganic salt solutions other than ammonium salt solutions} · CPC title
by acid leaching · CPC title
by an alkaline or ammoniacal leaching · CPC title
Working-up flue dust · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.