Aqueous waste vitrification process and apparatus

• US 4,666,490 A
• Filed: 02/12/1986
• Issued: 05/19/1987
• Est. Priority Date: 02/12/1986
• Status: Expired due to Fees

• Current Assignee: Ronald N. Drake
• Original Assignee: Ronald N. Drake
• Inventors: Drake, Ronald N.
• Primary Examiner(s): NOT, DEFINED
• Application Number:
  US06/828,857
• Time in Patent Office: 461 Days
• Field of Search: 65/45, 65/62, 65/181, 65/19, 65/27, 65/168, 65/134
• US Class Current: 588/256
• 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 5/235 Heating the glass C03B5/02, C03B5/18, C03B5/225 take precedence
• 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: Y10S 588/90 Apparatus

Abstract

A process is provided for treating an aqueous stream of nonradioactive hazardous waste containing inorganic compounds capable of forming oxides upon thermal treatment in which at least one of the oxides is a glass former, glass intermediate or a glass modifier. The process comprises (a) introducing the waste stream into a thermal treatment zone; (b) heating the inorganic compounds in the thermal treatment zone to convert the compounds to the corresponding inorganic oxides and form a melt solution while vaporizing volatile components to form an off-gas; (c) scrubbing the off-gas to provide a ventable flue gas and a liquid condensate with the condensate being recycled to the thermal treatment zone; and (d) removing the melt solution from said thermal treatment zone and cooling the melt solution to form a nonleachable glass containing the hazardous waste. An apparatus particularly adapted to practice the process is also provided.

Claims

1. A process for the treatment of an aqueous waste stream of nonradioactive waste containing at least one inorganic compound comprising a hazardous metal cation capable of forming an oxide upon thermal treatment, wherein said oxide is a glass former, glass intermediate, or glass modifier, said process comprising:

(a) introducing said waste stream into a thermal treatment zone;

(b) heating said inorganic compound in said thermal treatment zone to convert said compound to the corresponding inorganic oxide and form a melt solution while vaporizing volatile components to form an off-gas;

(c) scrubbing said off-gas to provide a ventable flue gas and a liquid condensate; and

(d) removing said melt solution from said thermal treatment zone and cooling said solution to form a nonhazardous glass encapsulating the hazardous metal cation.

2. The process of claim 1 wherein a material selected from the group consisting of a glass former, a glass modifier, a glass intermediate, and mixtures thereof is introduced into said thermal treatment zone independent of said waste stream.

3. The process of claim 1 wherein a material selected from the group consisting of a glass former, a glass modifier, a glass intermediate, and mixtures thereof is combined with said aqueous waste stream before said stream is introduced into said thermal treatment zone.

4. The process of claim 1 wherein said off-gas is scrubbed with a caustic solution to remove acid gases and provide a condensate which is recycled to said heating zone.

5. The process of claim 1 wherein said hazardous waste contains up to about 10 weight percent cyanide said cyanide being decomposed in said thermal treating zone.

6. The process of claim 1 wherein said waste stream is heated in said thermal treatment zone to form a crust phase and a melt phase, said crust phase being on top of said melt phase and having a lower temperature than said melt phase.

7. The process of claim 6 wherein said waste stream is heated in said thermal treatment zone to form a melt phase, a crust phase and an aqueous phase.

8. The process of claim 7 wherein said stream is continuously introduced into said thermal treatment zone wherein liquid vaporizes from said aqueous phase depositing solids on said crust phase and solids from said crust phase are dissolved into said molten phase.

9. The process of claim 7 wherein a material selected from the group consisting of a glass former, a glass modifier, a glass intermediate and mixtures thereof is added to said thermal treatment zone to provide a melt composition which forms a nonleachable glass when cooled.

10. The process of claim 9 wherein said glass former is selected from the group consisting of glass frit, B₂ O₃, SiO₂, GeO₂, P₂ O₅, V₂ O₅, and As₂ O₃.

11. The process of claim 9 wherein said glass modifier is selected from the group consisting of MgO, Li₂ O, BaO, CaO, SrO, Na₂ O, and K₂ O.

12. The process of claim 9 wherein said glass intermediate is selected from the group consisting of Al₂ O₃, Sb₂ O₃, ZrO₂, TiO₂, PbO, BeO, and ZnO.

13. A process for the treatment of an aqueous hazardous waste stream containing at least one inorganic compound whose thermal decomposition product is an oxide which is a glass former, glass modifier or glass intermediate which process comprises:

(a) introducing said stream into a thermal treatment zone;

(b) heating said stream in said thermal treatment zone to form a melt phase, a crust phase, and an aqueous phase;

(c) converting said inorganic compound to said oxide and concentrating said oxide in said melt;

(d) evaporating volatiles from said phases to form an off-gas;

(e) scrubbing said off-gas to provide a ventable flue gas and a condensate;

(f) returning said condensate to said thermal treatment zone; and

(g) removing said melt from said thermal treatment zone and cooling said melt to form a glass.

14. The process of claim 13 wherein a material selected from the group consisting of a glass former, a glass intermediate, a glass modifier, and mixtures thereof is combined with said waste stream.

15. The process of claim 14 wherein said inorganic compound is selected from the group consisting of Ni, Hg, Pb, Co, Au, Ag, Cr, Cd, Se, Sb, As, and Cu, the temperature of said melt phase is between about 1000°

C. and 1400°

C.

16. The process of claim 15 wherein a glass former selected from the group consisting of SiO₂, P₂ O₅, and mixtures thereof is combined with said waste stream.

17. The process of claim 13 wherein said waste stream contains a plurality of inorganic compounds.

18. An apparatus for the treatment of an aqueous waste stream of nonradioactive hazardous waste containing at least one inorganic compound capable of forming an oxide upon thermal treatment, said apparatus comprising:

(a) a means for mixing tne waste stream with a material selected from the group consisting of a glass former, a glass intermediate, a glass modifier, and mixtures thereof to form a combined stream;

(b) a means for heating said combined stream to form a melt phase with a crust phase thereon, wherein said oxide is concentrated in said melt phase and said melt phase is of a higher temperature than said crust phase, and wherein volatiles are being evolved from said phases;

(c) a means for transferring said combined stream from said mixing means to said heating means;

(d) a scrubbing means adapted to receive said volatiles from said heating means and scrub said volatiles with a caustic solution to form a condensate which is recycled to said heating means and a flue gas which is vented from said scrubbing means;

(e) a means for providing said caustic solution to said scrubbing means;

(f) a condensing means for receiving said flue gas from said scrubbing means and forming a condensate and a vent gas; and

(g) a means for receiving the melt from said heating means and cooling said melt to form solid shapes.