Sustainable method for recycling smelting works dusts and sludges to produce iron-containing, heavy-metal-depleted reclaimed materials with recovery of lead and zinc

Patent metadata

Field	Value
Publication number	US-12448666-B2
Application number	US-202117798709-A
Country	US
Kind code	B2
Filing date	Feb 25, 2021
Priority date	Feb 28, 2020
Publication date	Oct 21, 2025
Grant date	Oct 21, 2025

Abstract

The present invention relates to a sustainable regeneration process for metallurgical plant dusts and sludges for producing iron-containing, heavy metal-depleted secondary raw materials and recovering lead and zinc, by providing a first starting material which comprises at least one iron, zinc, lead and further heavy metal components containing metallurgical plant dust and/or sludge, and a second starting material containing at least one chlorine component, mixing the starting materials and drying the mixture, pyrolyzing the mixture for expelling zinc, lead and further heavy metal components, capturing the gas phase of the pyrolysis in sulfuric acid, and providing the residue which remains as an iron-containing secondary raw material depleted in zinc, lead and further heavy metal components.

First claim

The invention claimed is:

1. A regeneration process for producing iron-containing heavy metal-depleted secondary raw materials and recovering lead components and zinc components from at least one of metallurgical plant dust and sludge, comprising the steps of:
I) providing a first starting material which comprises at least one of iron, zinc, and lead, and a second starting material containing at least one chlorine component,
II) mixing the first starting material with the second starting material, transferring the mixture to an oven unit, and subsequently pelletizing it,
III) drying the mixture with expulsion of steam, and subsequently pelletizing it,
IV) reacting zinc, lead and further heavy metal components and chlorine components by pyrolysis,
V) capturing the gas phase from the pyrolysis from step IV) in sulfuric acid, with cooling,
V-a1) subsequent to step V) the sulfuric acid solution containing Zn in the form of ions is transferred to a further vessel and heated for removing residual chloride until the sulfuric acid fumes off,
V-a2) the sulfuric acid solution containing Zn in the form of ions from step V-a1) is cooled and transferred to a container with water, sulfuric acid and metallic zinc,
V-c1) PbSO4 from step V) is taken off as a solid,

VI) providing the pyrolysis residue which remains as an iron-containing secondary raw material depleted in zinc, lead and further heavy metal components.

2. The process of claim 1 , wherein SO3 is formed and expelled in step V-a1) and is one of captured and returned to step V) or into a corresponding vessel.

3. The process of claim 2 wherein in step V-a2) heavy metals selected from the group containing As, Cd, Pb and Sn are deposited on the Zn surface by electrolytic cementation.

4. The process of claim 3 wherein pure zinc is produced by electrolytic reduction in a step V-a3) from the sulfuric acid solution containing Zn in the form of ions from step V-a2).

5. The process of claim 3 , wherein the sulfuric acid solution containing Zn in the form of ions in step V-a2), after deposition of the heavy metals, is used as an electrolyte in a zinc coating plant.

6. The process of claim 5 wherein hydrogen chloride is expelled in step V and subsequent to step V) the hydrogen chloride expelled is introduced into water in a step V-b1) to form hydrochloric acid.

7. The process of claim 6 wherein the PbSO4 taken off as a solid in step V-c1) is filtered.

8. The process of claim 7 wherein the metallurgical plant dust and/or sludge used comprises at least one substance selected from the group containing converter dust, coke dust, blast furnace dust, blast furnace sludge, dust from secondary metallurgy, sintering dust, mill scale, mill scale sludge, zinc slags, copper industry slags, oil-containing sludges, electric arc furnace dust (EAF dust), hall dusts from electric steelworks, filter dusts, oxygen furnace dust and blast furnace throat sludge.

9. The process of claim 8 wherein as chlorine component at least one substance selected from the group containing hydrogen chloride, hydrochloric acid, Cl2, PVC, PCB, PCT, oils containing PCB or PCT, preferably hydrochloric acid, more preferably hydrochloric acid pickle is used.

10. The process of claim 9 wherein the steam expelled in step III) is condensed and the water is captured.

11. The process of claim 10 , wherein the hydrogen chloride expelled is introduced into the water condensed from the steam, and is used as regenerated hydrochloric acid.

12. The process of claim 11 wherein the process is carried out one of continuously or discontinuously.

13. The process of claim 11 wherein the basicity of the iron-enriched, heavy metal-depleted secondary raw material is adjusted by admixing CaO to at least one of the starting materials or mixture thereof.

14. The process of claim 13 wherein the secondary raw material from step VI) is iron-enriched.

15. The process of claim 14 wherein at least one starting material comprises alkali metal components and the secondary raw material is alkali metal component-depleted in comparison to the starting material, with the alkali metal components passing through the process together with the zinc and further heavy metal components.

16. The process of claim 8 wherein the metallurgical plant dust and/or sludge used comprises at least one substance selected from the group containing metallurgical plant dust and/or sludge from secondary iron/steel production.

17. The process of claim 8 wherein the metallurgical plant dust and/or sludge used comprises at least one substance selected from the group containing blast furnace throat sludge and/or oxygen furnace dust.

18. The process of claim 9 wherein the chlorine component includes hydrochloric acid pickle.

19. The process of claim 1 wherein the first starting material further comprises heavy metal components containing metallurgical plant dust and/or sludge.

Assignees

• Thyssenkrupp Steel Europe Ag

Inventors

• Tebeck Andreas
• Pappert Eckhard

Classifications

• C25D3/22

  of zinc · CPC title

• C25C1/16

  of zinc, cadmium or mercury · CPC title

• C22B19/30

  from metallic residues or scraps · CPC title

• C22B19/26

  Refining solutions containing zinc values, e.g. obtained by leaching zinc ores (treatment or purification of solutions by liquid-liquid extraction, by ion exchange or by adsorption C22B3/00) · CPC title

• C22B1/26

  Cooling of roasted, sintered, or agglomerated ores · CPC title