Method of indirect chemical reduction of metals in waste

• US 5,358,549 A
• Filed: 03/19/1993
• Issued: 10/25/1994
• 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:
  US08/033,846
• Time in Patent Office: 585 Days
• Field of Search: 75/414, 423/5
• 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 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 dissolved intermediate. 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-containing intermediate formed to dissolve 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, the 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; and

thereafter

b) exposing the metal of the metal-containing intermediate to a second reducing agent in the molten metal bath, the second reducing agent, under the operating conditions of the bath, chemically reducing said metal 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-containing intermediate formed to dissolve in the molten metal bath for subsequent reduction of the metal component of said intermediate, thereby indirectly reducing the component of the waste.

2. A method of claim 1 wherein the first reducing agent is a component of the molten metal bath.

3. A method of claim 1 wherein the second reducing agent is directed into the molten metal bath at a rate which is sufficient, relative to the rate at which the metal-containing intermediate is formed, to cause essentially all of said intermediate formed to dissolve in the molten metal bath.

4. A method of claim 3 wherein the second reducing agent 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 reduction of the metal of said intermediate by the second reducing agent.

5. A method of claim 4 wherein the second reducing agent and the metal of said component are directed into the molten metal bath at a stoichiometric ratio of about 1:

1.

6. A method of claim 5 wherein the stoichiometric ratio of the first reducing agent in the molten metal bath, to the metal of the component of the waste, is greater than about 1:

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

1.

7. A method of claim 3 wherein the waste and the second reducing agent 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 reduction of the metal of said intermediate by the second reducing agent.

8. A method of claim 1 wherein the waste includes more than one component which can be reduced by the first reducing agent in the molten metal bath.

9. A method of claim 8 wherein a metal component, which comprises a substantial portion of the molten metal bath, is also a metal component of the intermediate.

10. A method of claim 9 wherein the first reducing agent includes a metal in its elemental state.

11. A method of claim 10 further including the step of dissociating an organic component of the metal-containing composition to its respective elements.

12. A method of claim 1 wherein the second reducing agent includes carbon.

13. A method of claim 1 further including the steps of volatilizing the metal of the intermediate and then recovering the metal.

14. A method of claim 1 wherein the component is present in a sludge.

15. A method of claim 1 wherein the component is present in an ash.

16. A method of claim 1 wherein the component is present in a dust.

17. A method of claim 1 wherein the component is present in a soil.

18. A method of claim 1 wherein the component is a precious metal.

19. A method of claim 18 wherein the precious metal is selected from the group consisting essentially of titanium, vanadium, niobium, chromium, cobalt, nickel, silver and platinum.

20. A method of claim 1 wherein the component is a volatile heavy metal.

21. A method of claim 20 wherein the heavy metal is selected from the group consisting essentially of lead, mercury, cadmium, zinc, tin, and arsenic.

22. A method of claim 1 wherein the component is iron or copper.

23. A method of claim 22 wherein the oxygen-containing metal compound of the metal-containing waste composition comprises a metal oxychloride.

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

25. 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.

26. A method of claim 25 wherein the sacrificial metal is selected from the group consisting of aluminum, magnesium, calcium, silicon, and mixtures thereof.

27. A method for the indirect chemical reduction of at least two components of a waste, comprising the steps of:

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

b) exposing the metal of the intermediate to a second reducing agent in the molten metal bath, the second reducing agent, under the operating conditions of the molten metal bath, chemically reducing the intermediate at a rate, relative to the rate at which the first component of the waste is directed into the molten metal bath, which is sufficient to cause essentially all intermediate formed to dissolve in the molten metal bath for subsequent reduction of the metal component of the intermediate, thereby indirectly chemically reducing the first component of the waste; and

thereafter

c) directing a sacrificial metal into the molten metal bath after the second reducing agent has reduced the intermediate, the sacrificial metal being substantially 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 metal of a second component of the waste, the second component being substantially inert to the first and second reducing agents at the temperature of the molten metal bath, thereby chemically reducing the metal of the second component of the waste.

28. A method of claim 27, wherein the molten metal bath includes nickel, vanadium, chromium, and iron, and the waste includes at least one of a nickel metal, a nickel oxide at any nickel valence state, a nickel alkyl, and an oxygen-containing nickel organic complex.

29. A method of claim 27 wherein the molten metal bath includes iron and the waste comprises at least one of a nickel metal, a nickel oxide at any nickel valence state, a nickel alkyl, and an oxygen-containing nickel organic complex.

30. A method of claim 27 wherein the waste includes at least one radioactive metal.

31. A method of claim 27 wherein the waste includes at least one of a nickel metal, a nickel oxide at any nickel valence state, a nickel alkyl, and an oxygen-containing nickel organic complex.

32. A method of claim 31 wherein the element of the radioactive component is selected from the actinides group.

33. A method of claim 27 wherein the sacrificial metal is introduced into the molten metal bath at such an amount and rate as to combine with substantially all of the oxygen of the second oxygen-containing metal compound.

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

a) directing the waste into a molten metal bath, whereby a phase of the component is formed in the presence of a molten metal bath, the two phases being substantially immiscible, the molten metal bath including a-first reducing agent which, at the operating conditions of the molten metal bath, chemically reduces a significant portion of a metal of the component to form an intermediate and a reduced metal of said component at a surface of the molten metal bath which is in contact with the waste component phase, and wherein both the metal oxide and the reduced metal dissolve in the molten metal bath; and

b) directing a second reducing agent into the molten metal bath to chemically reduce the metal of the intermediate at a rate comparable to that of the dissolution of the reduced metal of the waste component into the molten metal bath.

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

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

b) exposing the metal of the metal-containing intermediate to a second reducing agent in the molten metal bath which, under the operating conditions of the bath, reduces said metal 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-containing intermediate formed to dissolve in the molten metal bath; and

thereafter

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