SYSTEM AND METHOD FOR RECOVERING METALS FROM A WASTE STREAM

• US 20170209870A1
• Filed: 05/22/2015
• Published: 07/27/2017
• Est. Priority Date: 05/22/2014
• Status: Abandoned Application

• Current Assignee: TAV Holdings Inc.
• Original Assignee: TAV Holdings Inc.
• Inventors: Valerio, Thomas
• Application Number:
  US15/313,494
• Publication Number:
  US 20170209870A1
• Time in Patent Office: Days
• CPC Class Codes: B02C 17/185 with more than one separator
• CPC Class Codes: B03B 5/623 Upward current classifiers
• CPC Class Codes: B03B 5/626 Helical separators
• CPC Class Codes: B03B 9/04 specially adapted for furnace residues, smeltings, or foundry slags
• CPC Class Codes: B03C 1/02 acting directly on the substance being separated
• CPC Class Codes: B03C 2201/20 Magnetic separation whereby the particles to be separated are in solid form
• CPC Class Codes: C22B 7/005 Separation by a physical processing technique only, e.g. by mechanical breaking
• CPC Class Codes: C22B 7/02 Working-up flue dust
• CPC Class Codes: Y02P 10/20 Recycling

Abstract

Devices, systems, and methods for recovering metal constituents from a waste stream containing metals (e.g., incinerator ash) are described. The waste stream may include incinerator bottom ash, fly ash, or a combination thereof. A falling velocity separator is employed in combination with a centrifuge to separate and collect metals from the waste stream. The falling velocity separator uses a liquid to separate particles within incinerator ash according to the particles settling velocities. The centrifuge further separates particles from the incinerator ash according to density of the particles.

Claims

1-25. -25. (canceled)

26. A system for separating a mixed waste stream containing metal, comprising:

a source of the mixed stream that is a slurry having incinerator bottom ash, fly ash, automotive shred residue, whitegood shredder residue, waste electronic and electronic equipment, or combinations thereof;

a first screen that receives the waste stream and separates the waste stream at a defined screen size into overs and unders, wherein the unders contains particles smaller than the defined screen size and the overs are greater than the defined size, wherein the screen size is less than 6 mm;

a size reducer for receiving the overs and for comminution of the overs;

a falling velocity separator that receives the unders, the falling velocity separator uses a liquid to separate the unders according to settling velocities of the particles into a first light fraction and a first heavy fraction;

a magnetic separator in communication with the falling velocity separator, the magnetic separator receives the first light fraction, and the magnetic separator removes ferrous particles from the first light fraction;

a centrifuge in communication with the magnetic separator, the centrifuge separates the first light fraction according to density of particles into a second material having a second light fraction and a second heavy fraction; and

a finishing table in communication with the centrifuge, the finishing table receives the second heavy fraction and concentrates the metals into precious metal and other metals.

27. The system of claim 26, wherein the size reducer is a wet ball mill.

28. The system of claims 27, wherein the falling velocity separator is an air-over-water pulsating jig.

29. The system of claims 26, wherein the falling velocity separator is a rising current classifier.

30. The system of claims 26, wherein the falling velocity separator is a screw separator.

31. The system of claim 28, wherein the screen size is about 1 mm.

32. The system of claim 29, further comprising a weir with an adjustable height.

33. The system of claim 32, further comprising a second screen having a second defined size, wherein the size is less than about 1 mm.

34. A method for recovering metals from a mixed waste stream containing the metals, comprising the steps of:

receiving the waste stream containing metals;

screening the waste steam into overs and unders according to a defined size;

size reducing the overs using wet ball mill;

separating the unders using a falling velocity separator to produce a first material containing a first heavy fraction and a first light fraction, wherein the falling velocity separator uses a liquid to separate the unders according to settling velocities of particles in the unders into the first light fraction and the first heavy fraction;

separating the first light fraction using a magnetic separator to produce a second material;

separating the second material using a centrifuge to produce a third material containing the metals;

concentrating the third material using a finishing table in precious metals and other metals.

35. The method of claim 34, wherein the falling velocity separator uses a fluid to produce the second material containing the metals.

36. The method of claim 34, wherein the fluid is water.

37. The method of claim 34, wherein the falling velocity separator separates the first material containing the desired metals by producing a hindered settling environment.

38. The method of claim 34, wherein the falling velocity separator is a pulsating jig.

39. The method of claim 34, wherein the falling velocity separator is a rising current classifier, or a screw separator.

40. The method of claim 34, wherein the falling velocity separator is a rising current classifier, or a screw separator.

41. The method of claim 34, wherein the waste stream contains is a slurry of incinerator bottom ash, fly ash, automotive shred residue, whitegood shredder residue, waste electronic and electronic equipment, or combinations thereof.

42. A method for recovering metals from a mixed waste stream containing the metals, comprising the steps of:

receiving the waste stream, wherein the waste stream contains is a slurry of incinerator bottom ash, fly ash, automotive shred residue, whitegood shredder residue, waste electronic and electronic equipment, or combinations thereof;

screening the waste stream into overs and unders according to a defined size, wherein the unders are sized less than 6 mm;

screening the unders with a second screen of less than 1 mm to remove a fraction less than 1 mm;

size reducing the overs using a wet ball mill;

separating the unders using a falling velocity separator to produce a first material containing a heavy fraction and a light fraction, wherein the falling velocity separator uses a liquid to separate the unders according to settling velocities of particles into a first light fraction and a first heavy fraction

separating the light fraction using a magnetic separator to produce a second material that is substantially free of ferrous metals;

separating the second material using a centrifuge to produce a third material containing a metal concentrate; and

separating the metal concentrate using a finishing table into a precious metal, heavy concentrate, a light material

separating the light material using the finishing table.

43. The method of claim 42, wherein the falling velocity separator is a pulsating jig.

44. The method of claim 42, wherein the falling velocity separator is a rising current classifier or a screw separator.