Method for waste vitrification

• US 7,108,808 B1
• Filed: 04/18/1990
• Issued: 09/19/2006
• Est. Priority Date: 04/18/1990
• Status: Active Grant

• Current Assignee: Stir-Melter Incorporated
• Original Assignee: Stir-Melter Incorporated
• Inventors: Richards, Ray S.
• Primary Examiner(s): MAI, NGOCLAN THI
• Application Number:
  US07/510,556
• Time in Patent Office: 5,998 Days
• Field of Search: 252/628, 252/629, 204/1.5, 373/29, 373/36, 373/39, 373/41
• US Class Current: 588/11
• CPC Class Codes: C03B 5/005 of glass-forming waste materials disposal or transformation of solid waste in general B09B; treatment of radioactive waste G21F9/00
• CPC Class Codes: C03B 5/027 by passing an electric current between electrodes immersed in the glass bath, i.e. by direct resistance heating
• CPC Class Codes: C03B 5/033 by using resistance heaters above or in the glass bath, i.e. by indirect resistance heating
• CPC Class Codes: C03B 5/1875 of the screw or pump-action type
• CPC Class Codes: C03B 5/26 Outlets , e.g. drains, siphons; Overflows , e.g. for supplying the float tank, tweels
• CPC Class Codes: C03B 5/265 Overflows; Lips; Tweels
• CPC Class Codes: G21F 9/305 Glass or glass like matrix C03B5/005 takes precedence; compositional aspects C03C
• CPC Class Codes: Y02P 40/50 Glass production, e.g. reusing waste heat during processing or shaping
• CPC Class Codes: Y02P 40/57 Improving the yield, e-g- reduction of reject rates

Abstract

A waste vitrification apparatus (10) having rotatable mixer impeller (16) functioning as a shaft electrode (60) and metallic vessel (14) functioning as a vessel electrode (62). A stream (12) of waste material and vitrifiable material are mixed and melted in the vessel (14) for vitrification. The waste vitrification method converts a feed stream (12) by mixing the feed stream into a glass melt (13) and melting glass batch of the feed stream (12) to form a foamy mass. The stream is dispersed by the impeller (16) to form a foam which is then densified in a settling zone (22), recovered through a spout (24) and solidified in storage containers. Means are provided to adjust the location of the mixing impeller (16) in the vessel (14) to change the depth of the settling zone (22). The impeller (16) is mounted on a drive shaft (18) having a recirculating coolant flow.

Claims

1. A waste vitrification method performed at least in part in a vessel having a wall and a rotatable impeller comprising the steps of:

introducing a feed stream comprising waste material into the vessel;

mixing the feed stream into a glass melt formed in the vessel with the impeller to disperse said feed stream in the melt to form a foamy mass, said foamy mass comprising gaseous material released by the waste material into the glass melt;

completing an electrical circuit between the wall of the vessel and the impeller and including said foamy mass to form a molten vitrified output;

densifying the foamy mass by passing said foamy mass into a quiescent zone where a portion of the gaseous material in said foamy mass separates from said foamy mass to form a molten vitrifiable output; and

recovering the molten vitrified output.

2. The waste vitrification method of claim 1 wherein said feed stream further comprises glass batch in solid form.

3. The waste vitrification method of claim 1 wherein said feed stream is an aqueous mixture.

4. The waste vitrification method of claim 3 wherein said feed stream is approximately 60 percent water and 40 percent solids by weight.

5. The waste vitrification method of claim 4 wherein said solids include frit.

6. The waste vitrification method of claim 2 wherein said feed stream comprises a first feed stream of waste materials and a second feed stream of glass batch in solid form.

7. The waste vitrification method of claim 1 wherein said step of mixing is performed by an impeller having outer surface portion moving at a speed of more than 250 feet per minute.

8. The waste vitrification method of claim 1 wherein said step of mixing is performed by an impeller having outer surface portion moving at a speed of more than 500 feet per minute.

9. The waste vitrification method of claim 1 wherein said steps of mixing and heating the foamed material are performed simultaneously in the vessel.

10. The method of claim 1 wherein said heating continues through the densifying step to maintain the molten vitrified output in a pourable state until after the recovering step.

11. The the method of claim 1, further comprising the step of cooling the molten vitrified output to form a solidified vitreous mass.

12. The method of claim 1 wherein said feed stream includes radioactive material.

13. The method of claim 1 wherein said glass batch material is boro-silicate glass.

14. A waste vitrification method performed at least in part in a vessel having a wall and a rotatable impeller comprising the steps of:

introducing a mixture of solid waste material and glass batch into the vessel;

mixing the mixture in the vessel with the impeller to form a foamy mass comprising gaseous material released by the waste material into the glass melt;

completing an electrical circuit from the wall of the vessel through said foamy mass to said impeller to provide heat which forms a molten vitrified output;

densifying the foamy mass by passing the foamy mass into a quiescent zone where the foamy mass separates into a densified portion and a gaseous portion; and

recovering the densified portion.

15. The waste vitrification method of claim 14 wherein said steps of mixing and heating the foam material are performed simultaneously in the vessel.

16. The method of claim 14 wherein residual heat is maintained through the densifying step to keep the densified material in a pourable state until after the recovering step.

17. A waste vitrification method performed at least in part in the vessel having a wall and a rotatable impeller comprising the steps of:

introducing a mixture of solid waste material and glass batch material into the vessel;

mixing the mixture in the vessel with the impeller to form a foamy mass comprising solid waste material, glass batch material and gaseous material released by said solid waste material and glass batch material;

completing an electrical series circuit relationship including the wall of the vessel, the foamy mass and the impeller;

densifying the foamy mass by passing the foamy mass into a quiescent zone where the foamy mass separates into a densified portion and a gaseous portion; and

recovering the densified portion.