Method for indirect chemical reduction of metals in waste

• US 5,322,547 A
• Filed: 03/19/1993
• Issued: 06/21/1994
• Est. Priority Date: 05/05/1992
• Status: Expired due to Term

• Current Assignee: Quantum Catalytics LLC
• Original Assignee: Molten Metal Technology Incorporated
• Inventors: Nagel, Christopher J., Bach, Robert D.
• Primary Examiner(s): ROSENBERG, PETER
• Application Number:
  US08/034,557
• Time in Patent Office: 459 Days
• Field of Search: 75/414, 423/5, 110/346, 588/201
• US Class Current: 75/414
• CPC Class Codes: A62D 2101/08 Toxic combustion residues, e.g. toxic substances contained in fly ash from waste incineration
• CPC Class Codes: A62D 2101/20 Organic substances
• CPC Class Codes: A62D 2101/40 Inorganic substances
• CPC Class Codes: A62D 2101/43 containing heavy metals, in the bonded or free state
• CPC Class Codes: A62D 3/32 by treatment in molten chemical reagent, e.g. salts or metals
• CPC Class Codes: B09C 1/06 thermally
• CPC Class Codes: B09C 1/067 by vitrification
• CPC Class Codes: C22B 5/02 Dry methods smelting of sulfides or formation of mattes
• CPC Class Codes: C22B 7/001 Dry processes
• CPC Class Codes: C22B 7/04 Working-up slag
• CPC Class Codes: Y02P 10/20 Recycling
• CPC Class Codes: Y10S 423/12 Molten media

Abstract

An environmentally sound process is described for the remediation of waste materials that allows the separation, recovery and decontamination of metals. The method includes chemically reducing essentially all of a reducible toxic and potentially hazardous metal-containing component of a waste composition. The waste is directed into a molten metal bath, including a first reducing agent which, under the operating conditions of the molten metal bath, chemically reduces a metal of the metal-containing component to form a dissolved intermediate. A reagent is directed into the molten metal bath for metal-ligand exchange with the dissolved intermediate to form a metal-ligand exchange product that includes the metal of the dissolved intermediate. A second reducing agent is directed into the molten metal bath. The second reducing agent, under the operations of the molten metal bath, chemically reduces the metal of the metal-ligand exchange product. The rate at which the second reducing agent is directed into the molten metal bath, relative to the rate at which the component of the waste is directed into the molten metal bath, is sufficient to cause essentially all metal of the metal-containing intermediate formed to be reduced in the molten metal bath, thereby indirectly chemically reducing the component of the waste. This indirect reduction technology can remediate a variety of materials, including ash metal-contaminated municipal waste, vitreous slag-like materials and spent metal catalysts, while allowing the recovery of remediable metals.

Claims

1. A method for indirect chemical reduction of a component of a waste, comprising the steps of:

a) directing the waste, containing the component, into a molten metal bath, including a metal-containing first reducing agent which, under the operating conditions of the molten metal bath, chemically reduces said component of the waste to form a dissolved metal-containing intermediate;

b) directing a metal-ligand exchange reagent into the molten metal bath, said metal-ligand exchange reagent causing a metal-ligand exchange reaction with the metal-containing intermediate to form a metal-ligand exchange product which includes the metal of the intermediate; and

c) exposing the metal-ligand exchange product to a second reducing agent in the molten metal bath which, under the operating conditions of the bath, chemically reduces the metal of the metal-ligand exchange product at a rate, relative to the rate at which the component of the waste is directed into the molten metal bath, which is sufficient to cause essentially all metal of the metal-containing intermediate formed to be reduced in the molten metal bath, thereby indirectly reducing the component of the waste.

2. A method of claim 1 wherein a ligand of the intermediate is an oxygen-containing ligand.

3. A method of claim 1 wherein a ligand of the intermediate is a sulphur-containing ligand.

4. A method of claim 1 wherein a ligand of the intermediate is a phosphorous-containing ligand.

5. A method of claim 1 wherein a ligand of the intermediate is a nitrogen-containing ligand.

6. A method of claim 1 wherein a ligand of the intermediate is a halogen-containing ligand.

7. A method of claim 1 wherein the molten metal bath is comprised substantially of the first reducing agent.

8. A method of claim 1 wherein the metal-ligand exchange reagent is directed into the molten metal bath at a stoichiometric ratio to the rate at which the metal of the waste component is directed into said bath which is at least about 1:

1.

9. A method of claim 8 wherein the metal-ligand exchange reagent is directed into the molten metal bath at a location which is sufficiently remote from a point of introduction of the waste to cause essentially all of the metal-containing intermediate formed in the molten metal bath to dissolve prior to metal-ligand exchange of said intermediate by the metal-ligand exchange reagent.

10. A method of claim 8 wherein the waste and the metal-ligand exchange reagent are directed into the molten metal bath at alternating intervals, whereby essentially all of the metal-containing intermediate formed in the molten metal bath dissolves prior to metal-ligand exchange of the metal of said intermediate by the second reducing agent.

11. A method of claim 1 wherein the metal of the metal-containing component is a precious metal.

12. A method of claim 11 wherein the precious metal is selected from the group consisting essentially of titanium, vanadium, niobium, chromium, cobalt, nickel, silver and platinum.

13. A method of claim 1 wherein the metal of the metal-containing component is a volatilizable heavy metal.

14. A method of claim 13 wherein the heavy metal is selected from the group consisting essentially of lead, mercury, cadmium, zinc, tin, and arsenic.

15. A method of claim 1 wherein the metal of the metal-containing component is iron or copper.

16. A method of claim 15 wherein the metal-containing component of the waste composition includes an organic component.

17. A method of claim 1 wherein the second reducing agent is a metal.

18. A method of claim 17 wherein the stoichiometric ratio of the first reducing agent to the metal of the component is greater than about 1:

1 and the stoichiometric ratio of the second reducing agent to the metal of the intermediate is greater than about 1;

1.

19. A method of claim 18 wherein the waste includes more than one component which can be reduced by the first reducing agent in the molten metal bath.

20. A method of claim 19 wherein a metal component which comprises a substantial portion of the molten bath is also a metal component of the intermediate.

21. A method of claim 19 wherein the first reducing agent includes a metal in its elemental state.

22. A method of claim 21 further including the step of dissociating an organic component of the waste, to its respective elements.

23. A method of claim 22 wherein the second reducing agent includes carbon.

24. A method of claim 23 further including the steps of volatilizing the metal of the intermediate and then recovering the metal.

25. A method of claim 24 wherein the component is present in a sludge.

26. A method of claim 24 wherein the component is present in an ash.

27. A method of claim 24 wherein the component is present in a dust.

28. A method of claim 24 wherein the component is present in a soil.

29. A method of claim 1 further including the step of directing a sacrificial metal into the molten metal bath after the second reducing agent has reduced at least a significant portion of the intermediate, the sacrificial metal being soluble in the molten metal bath and having a lower free energy of oxidation than the second reducing agent, whereby the sacrificial metal reacts with a second component of the waste composition which is substantially inert to the first and second reducing agents at the temperature of the molten metal bath.

30. A method of claim 29 wherein the sacrificial metal is selected from the group consisting of aluminum, magnesium, calcium, silicon, and mixtures thereof.

31. A method of claim 30, wherein the molten metal bath includes nickel, vanadium, chromium, and iron, and the waste composition includes a sulfide, phosphide, nitride, oxide or halide.

32. A method of claim 30 wherein the molten metal bath includes iron and the waste composition includes a sulfide, phosphide, nitride, oxide or halide.

33. A method of claim 30 wherein the molten metal bath includes at least one radioactive metal.

34. A method of claim 30 wherein the waste composition includes a sulfide, phosphide, nitride, oxide or halide.

35. A method of claim 34 wherein the element of the radioactive component is selected from the actinides group.

36. A method of claim 30 wherein the sacrificial metal is introduced in the molten metal bath at a rate which is sufficient to combine with substantially all of the second component.

37. A method for chemically remediating a metal-containing component of a waste, comprising the steps of:

a) directing the waste, containing the component, into a molten metal bath, including a metal-containing first reducing agent which, under the operating conditions of the molten bath, chemically reduces said component of the waste to form a dissolved metal-containing intermediate;

b) directing a metal-ligand exchange reagent into the molten metal bath, said metal-ligand exchange reagent causing a metal-ligand exchange reaction with the metal-containing intermediate to form a metal-ligand exchange product which includes the metal of the intermediate;

c) exposing the metal-ligand exchange product to a second reducing agent in the molten metal bath which, under the operating conditions of the bath, chemically reduces the metal of the metal-ligand exchange product at a rate, relative to the rate at which the component of the waste is directed into the molten metal bath, which is sufficient to cause essentially all metal of the metal-containing intermediate formed to be reduced in the molten metal bath; and

thereafter

d) reclaiming the reduced metal component of the waste from the molten metal bath.