ENRICHMENT PROCESS FOR A PGM-METALS CONTAINING STREAM

• US 20100213133A1
• Filed: 07/28/2008
• Published: 08/26/2010
• Est. Priority Date: 07/27/2007
• Status: Active Grant

• Current Assignee: Tshwane University of Technology
• Original Assignee: Tshwane University of Technology
• Inventors: Kasaini, Henry
• Granted Patent: US 8,168,069 B2
• Time in Patent Office: Days
• US Class Current: 210/674
• CPC Class Codes: B01D 15/00 Separating processes involving the treatment of liquids with solid sorbents using liquid sorbents B01D11/00; ion exchange processes or materials, sorbent materials in general B01J, e.g. sorbents for chromatography B01J20/281; for investigating or analysing materials G01N30/00; Apparatus therefor
• CPC Class Codes: C22B 11/04 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 Class Codes: C22B 11/06 Chloridising
• CPC Class Codes: C22B 3/10 Hydrochloric acid , other halogenated acids or salts thereof
• CPC Class Codes: C22B 3/24 by adsorption on solid substances, e.g. by extraction with solid resins
• CPC Class Codes: Y02P 10/20 Recycling

Abstract

The invention provides an enrichment process for a PGM-group metals containing stream, said process including the steps of contacting activated carbon particles with a PGM-rich stream by contacting the stream with a batch of the particles on a continuous basis, whereby at least some of the PGM-group metals are adsorbed from the stream onto active surface sites of the activated carbon and a PGM-metals depleted stream passes out of contact with the activated carbon batch, thereafter stripping the PGM-group metals from the activated carbon batch by means of a concentrated HCl solution as stripping agent, wherein the stripping agent is contacted with the activated carbon batch on a continuous flow basis and the PGM-group metals loaded stripping agent is removed from contact with the activated carbon from which the PGM-group metals have been stripped, and then regenerating the activated carbon batch by washing with water and, if necessary, reactivating the carbon particles.

Claims

1-16. -16. (canceled)

17. An enrichment process for a stream containing platinum group metals, comprising:

contacting, on a continuous basis, a batch of activated carbon particles with a platinum group metal-containing stream, whereby at least a portion of the platinum group metal is adsorbed from the platinum group metal-containing stream onto active surface sites of the activated carbon particles so as to generate a platinum group metal-depleted stream;

passing the platinum group metal-depleted stream out of contact with the batch of activated carbon particles with adsorbed platinum group metal;

contacting, on a continuous basis, the batch of activated carbon particles with adsorbed platinum group metal to a concentrated HCl solution stripping agent, whereby a platinum group metal-loaded stripping agent is generated;

removing the platinum, group metal-loaded stripping agent from contact with the batch of activated carbon particles from which the platinum group metal has been stripped; and

regenerating the activated carbon particles from which the platinum group metal has been stripped by washing with water.

18. The enrichment process of claim 17, further comprising reactivating the batch of activated carbon particles after regenerating.

19. The enrichment process of claim 17, wherein contacting, on a continuous basis, a batch of activated carbon particles with a platinum group metal-containing stream occurs in an adsorption zone of an agitated carbon-in-reactor vessel.

20. The enrichment process of claim 19, wherein an oxygen rich stream is mixed with the platinum group metal-containing stream prior to or during contacting, on a continuous basis, the batch of activated carbon particles with the platinum group metal-containing stream.

21. The enrichment process of claim 20, wherein the oxygen rich stream is an oxygen containing gas stream which is bubbled into a mixture of the platinum group metal-containing stream and the batch of activated carbon particles in an adsorption zone.

22. The enrichment process of claim 20, wherein a rate of oxygen addition is sub-stoichiometric.

23. The enrichment process of claim 20, wherein a rate of oxygen addition is selected to achieve excess oxygen conditions.

24. The enrichment process of claim 17, wherein the batch of activated carbon particles is agitated in the platinum group metal-containing stream as the platinum group metal-containing stream through and around the activated carbon particles which are retained in the batch.

25. The enrichment process of claim 17, wherein the batch of activated carbon particles is in a bed with the platinum group metal-containing stream being passed over the bed in a continuous flow.

26. The enrichment process of claim 17, further comprising separating at least a portion of suspended solids from the platinum group metal-containing stream so as to reduce poisoning of the active surface sites of the activated carbon particles and/or to reduce blocking of pores of the activated carbon particles.

27. The enrichment process of claim 17, wherein a concentration of the concentrated HCl solution stripping agent is from 2 M to 5 M

28. The enrichment process of claim 17, wherein a concentration of the concentrated HCl solution stripping agent is from 3 M to 4 M.

29. The enrichment process of claim 17, wherein the activated carbon particles are amine treated activated carbon particles.

30. The enrichment process of claim 17, wherein washing comprises contacting washed activated carbon with an amine containing stream.

31. The enrichment process of claim 30, wherein amine containing stream is a primary amine containing stream or a secondary amine containing stream.

32. The enrichment process of claim 17, wherein the regenerated activated carbon particles are re-used, in-situ, in contacting the platinum group metal-containing stream, and wherein the platinum group metal-containing stream is fresh or recycled.

33. The enrichment process of claim 17, wherein a ratio of a concentration of platinum group metal in the platinum group metal-containing stream to the platinum group metal-loaded stripping agent is higher than 2.

34. The enrichment process of claim 17, wherein a ratio of a concentration of platinum group metal in the platinum group metal-containing stream to the platinum group metal-loaded stripping agent is about 10 or higher.

35. The enrichment process of claim 17, wherein the platinum group metal-depleted stream is discarded or further contacted with the batch of activated carbon particles.

36. The enrichment process of claim 17, wherein the platinum group metal-loaded stripping agent is recycled or taken for further processing.