Patent Number: 059096543
Section: claims

1. A method for the volume reduction of solid organic waste from nuclear facilities, said method comprising: (a) subjecting said organic waste to pyrolysis to form a gas which comprises organic compounds, said pyrolysis further forming a solid pyrolysis residue comprising residual carbon from said organic waste; and  (b) gasifying via steam reforming solid pyrolysis residue to extract at least a portion of said residual carbon.  (a) subjecting said organic waste to pyrolysis to form a first gas comprising organic compounds, said pyrolysis further forming a solid pyrolysis residue comprising residual carbon from said organic waste;  (b) gasifying via steam reforming said solid pyrolysis residue to extract at least a portion of said residual carbon, said gasification forming a second gas and a solid waste residue; and  (c) oxidizing said first gas and said second gas.  (a) adding iron powder to said solid organic waste;  (b) subjecting said organic waste to pyrolysis to form a gas which comprises organic compounds, said pyrolysis further forming a solid pyrolysis residue comprising residual carbon from said organic waste; and  (c) gasifying said solid pyrolysis residue to extract at least a portion of said residual carbon.  (a) subjecting said organic waste to pyrolysis to form a first gas comprising organic compounds, said pyrolysis further forming a solid pyrolysis residue comprising residual carbon from said organic waste;  (b) gasifying said solid pyrolysis residue to extract at least a portion of said residual carbon, said gasification forming a second gas and a solid waste residue; and  (c) oxidizing said first gas and said second gas in a submerged bed heater.  (a) subjecting said organic waste to pyrolysis to form a first gas comprising organic compounds, said pyrolysis further forming a solid pyrolysis residue comprising residual carbon from said organic waste;  (b) gasifying said solid pyrolysis residue to extract at least a portion of said residual carbon, said gasification forming a second gas and a solid waste residue;  (c) oxidizing said first gas and said second gas; and  (d) removing residual acid gases from said oxidized gases wherein said removal is performed by a fiber bed scrubber. 2. The method of claim 1 wherein said gasifying of said solid pyrolysis residue forms carbon dioxide and carbon monoxide. 3. The method for the volume reduction of solid organic waste of claim 1 wherein said pyrolysis is performed at a temperature of no more than 700.degree. C. 4. The method for the volume reduction of solid organic waste of claim 1 wherein said pyrolysis is carried out in the absence of a catalyst for the breaking down of carbon compounds that are present in said organic waste. 5. The method for the volume reduction of solid organic waste of claim 1 wherein said solid organic waste is an ion exchange medium. 6. The method for the volume reduction of solid organic waste of claim 3 wherein said pyrolysis is performed at a temperature of no more than 600.degree. C. 7. The method for the volume reduction of solid organic waste of claim 6 wherein said pyrolysis is performed at a temperature in the range of 450.degree. C. to 550.degree. C. 8. The method for the volume reduction of solid organic waste of claim 1 wherein said pyrolysis of said solid organic waste is performed for a residence time of less than 10 seconds. 9. The method for the volume reduction of solid organic waste of claim 8 wherein said pyrolysis of said solid organic waste is performed for a residence time of 5 to 8 seconds. 10. The method for the volume reduction of solid organic waste of claim 1 wherein said gasification of said solid pyrolysis residue reduces said solid pyrolysis residue by a factor of about 2 to 5 times. 11. The method of claim 1 further comprising the step of grinding said solid organic waste prior to pyrolysis. 12. The method of claim 11 further comprising the step of drying said ground organic waste prior to pyrolysis. 13. The method of claim 11 further comprising the step of adding iron powder to the ground organic waste prior to pyrolysis. 14. The method of claim 12 further comprising the step of adding iron powder to the dried ground organic waste powder prior to pyrolysis. 15. The method of claim 14 wherein said organic waste contains chlorine which combines with said iron powder to form FeCl.sub.2. 16. The method of claim 14 wherein said organic waste contains sulfur which combines with said iron powder to form FeS and FeS.sub.2. 17. The method for the volume reduction of solid organic waste of claim 1 wherein said solid pyrolysis residue comprises radioactive material. 18. A method for the processing of solid organic waste from nuclear facilities, said method comprising: 19. The method of claim 18 wherein said oxidizing step is performed in a submerged bed heater. 20. The method of claim 18 further comprising the step of grinding said organic waste. 21. The method of claim 20 further comprising the step of drying said organic waste. 22. The method of claim 20 further comprising the step of adding iron powder to said ground organic waste. 23. The method of claim 22 wherein said organic waste contains sulfur which combines with said iron powder to form FeS. 24. The method of claim 22 wherein said organic waste contains sulfur which combines with said iron powder to form FeS.sub.2. 25. The method of claim 22 wherein said organic waste contains chlorine which combines with said iron powder to form FeCl. 26. The method of claim 18 further comprising the step of quickly reducing the temperature of the oxidized gases of step (c). 27. The method of claim 26 further comprising the step of removing residual acid gases from said reduced temperature oxidized gases. 28. The method of claim 27 wherein said removal of residual acid gases is performed by a fiber bed scrubber. 29. The method for the volume reduction of solid organic waste of claim 1, wherein said organic waste contains up to about 50 percent moisture content. 30. The method for the volume reduction of solid organic waste of claim 29, wherein said organic waste contains from about 10 to about 30 percent moisture content. 31. The method for the volume reduction of solid organic waste of claim 1, wherein said pyrolysis of said organic waste is performed in the presence of substoichiometric quantities of oxygen. 32. A method for the volume reduction of solid organic waste from nuclear facilities, said method comprising: 33. The method of claim 32 further comprising the step of grinding said solid organic waste prior to pyrolysis. 34. The method of claim 32 further comprising the step of drying said solid organic waste prior to pyrolysis. 35. The method of claim 32 wherein said organic waste contains chlorine which combines with said iron powder to form FeCl.sub.2. 36. The method of claim 32 wherein said organic waste contains sulfur which combines with said iron powder to form FeS and FeS.sub.2. 37. A method for the processing of solid organic waste from nuclear facilities, said method comprising: 38. A method for the processing of solid organic waste from nuclear facilities, said method comprising: 39. The method of claim 38 further comprising the step of quickly reducing the temperature of the oxidized gases.