Production of zinc oxide from complex sulfide concentrates using chloride processing

• US 6,395,242 B1
• Filed: 10/01/1999
• Issued: 05/28/2002
• Est. Priority Date: 10/01/1999
• Status: Expired due to Fees

• Current Assignee: Noranda, Inc. (Glencore Plc)
• Original Assignee: Noranda, Inc. (Glencore Plc)
• Inventors: Kondos, Peter, Van Sandwijk, Anthonie, Payant, Serge, Allen, Carole, Van Weert, Gezinus
• Primary Examiner(s): BOS, STEVEN J
• Application Number:
  US09/410,102
• Time in Patent Office: 970 Days
• Field of Search: 423/622,109,140,141,142,104,101,102,481,155,639,488,38,39,150.1,98 75/726,733,738,724,725
• US Class Current: 423/101
• CPC Class Codes: C22B 19/22 with leaching with acids
• CPC Class Codes: C22B 19/26 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 Class Codes: C22B 19/34 Obtaining zinc oxide purifying zinc oxide C01G9/02
• CPC Class Codes: C22B 3/02 Apparatus therefor
• CPC Class Codes: C22B 3/10 Hydrochloric acid , other halogenated acids or salts thereof
• CPC Class Codes: C22B 7/02 Working-up flue dust
• CPC Class Codes: Y02P 10/20 Recycling

Abstract

The present invention relates to an apparatus and a process for producing zinc oxide from a zinc-bearing material. The process according to the present invention comprises the steps of leaching the complex sulfide material with hydrochloric acid and oxygen; precipitating iron from the leach solution using magnesium oxide and oxygen; removing copper, silver, cadmium, cobalt and lead from the leach solution by cementation with zinc dust; precipitating zinc oxide from the leach solution using magnesium oxide; and spray roasting the remaining magnesium chloride leach solution to regenerate hydrochloric acid and magnesium oxide. The present invention further relates to processes for recovering copper, silver, lead, and iron from complex sulfide materials.

Claims

1. A process for recovering (i) zinc oxide, (ii) iron, and (iii) at least one of copper, silver, cadmium, cobalt and lead from a material that includes zinc, iron, and at least one of copper, silver, cadmium, cobalt and lead, comprising the steps of:

leaching the material with hydrochloric acid and oxygen to produce a leach solution;

precipitating iron from the leach solution with magnesium oxide;

recovering at least one of copper, silver, cadmium, cobalt and lead from the leach solution by cementation with zinc dust; and

precipitating zinc oxide from the leach solution with magnesium oxide.

2. The process of claim 1, wherein the lead is precipitated from the leach solution as lead chloride, and is crystallized for recovery at a lead refinery.

3. The process of claim 1, wherein the cementation with zinc dust is carried out in two or more stages.

4. A process for producing zinc oxide from a material which contains (i) zinc, (ii) iron, and (iii) at least one of copper, silver, cadmium, cobalt and lead, the process comprising the steps of:

leaching the material with hydrochloric acid and oxygen to produce a leach solution;

precipitating iron from the leach solution with magnesium oxide;

recovering at least one of copper, silver, cadmium, cobalt and lead from the leach solution by cementation with zinc dust;

precipitating zinc oxide from the leach solution with magnesium oxide; and

spray roasting a magnesium chloride solution remaining after precipitating zinc oxide to regenerate hydrochloric acid and magnesium oxide.

5. The process of claim 4, further comprising the step of drying the zinc oxide precipitate.

6. The process of claim 4, further comprising the step of re-dissolving, purifying with zinc dust, and zinc sulfate electrowinning of the zinc oxide precipitate.

7. The process of claim 4, further comprising the step of removing additional trace elements from the solution during cementation.

8. The process of claim 4, wherein the leach solution has a temperature in the range of approximately 50 to 150°

C.

9. The process of claim 4, wherein the leach solution has a pH of 1 or lower.

10. The process of claim 4, wherein the zinc oxide precipitate has a chloride content of less than 0.1% by weight, and a magnesium content of less than 0.5% by weight.

11. The process of claim 4, wherein 90% by weight or more of zinc is extracted from the zinc-bearing material.

12. The process of claim 4, wherein the zinc-bearing material is a complex sulfide material.

13. The process of claim 12, wherein sulfide sulfur present in the complex sulfide material is transformed into elemental sulfur.

14. The process of claim 4, wherein the zinc-bearing material comprises a secondary material selected from the group consisting of EAF dust, BOF dust, and ferrites.

15. The process of claim 4, wherein the cementation with zinc dust is carried out in two or more stages.

16. The process of claim 4, wherein the leaching step is conducted as a single step.

17. The process of claim 4, wherein the leaching step is conducted as a continuous process having multiple HCl addition points.

18. The process of claim 4, further comprising an acid neutralization step to remove excess HCl from the leach solution.

19. The process of claim 4, wherein the leaching step includes the step of oxidizing iron.

20. The process of claim 4, wherein, in the leaching step, the material and the oxygen are added to maintain a redox potential between 250 and 600 mV.

21. The process of claim 4, wherein, in the precipitating zinc oxide step, the zinc is precipitated from the zinc chloride solution as zinc hydroxychloride.

22. The process of claim 21, wherein the precipitation is effected by addition of MgO.

23. The process of claim 21, wherein the precipitation is effected at a temperature between 50°

C. and 100°

C.

24. The process of claim 21, wherein the precipitation is effected at a pH between 4.0 and 9.0.

25. The process of claim 21, wherein zinc is partially removed from zinc chloride solution.

26. The process of claim 21, wherein a low magnesium zinc hydroxychloride is produced in the precipitating zinc oxide step.

27. The process of claim 21, wherein the zinc hydroxychloride is destabilized.

28. The process of claim 27, wherein the destabilization is effected on solids following a solid-liquid separation.

29. The process of claim 27, wherein the destabilization is effected at a temperature between 20 and 95°

C.

30. The process of claim 27, wherein the destabilization is effected at a pH between 7.66 and 12.

31. The Process of claim 27, wherein the destabilization is carried out by addition of one of lime, hydrated lime, and sodium hydroxide.

32. The process of claim 21, wherein the partial liquor, after a solid-liquid separation, is subjected to a secondary zinc precipitation step.

33. The process of claim 32, wherein the secondary zinc precipitation step is carried out at a temperature of from 50°

C. to 150°

C.

34. The process of claim 32, wherein the secondary zinc precipitation step is carried out at a pH of from 4.0 to 9.0.

35. The process of claim 32, wherein the recovered solids contain a portion of magnesium.

36. The process of claim 32, wherein the recovered solids are sent to the precipitating zinc oxide step.

37. The process of claim 4, wherein the material contains silver, and the amount of zinc dust added during the cementation step is adjusted to increase the amount of silver recovered from said material.