Patent Number: 
Section: claims

1. A method for immobilizing non-aqueous liquid radioactive waste, the method comprising:a) mixing the liquid waste with polymer to convert the liquid waste to a non liquid waste;b) contacting the non-liquid waste with sulfur to create a mixture;c) heating the mixture for a time and at a temperature to form homogeneous, chemically stable solid phase; andcompressing the chemically stable solid phase into a final waste monolith wherein the mixture is in step c subjected to temperatures below the flash point of the liquid radioactive waste. 2. A method for immobilizing non-aqueous liquid radioactive waste, the method comprising:a) mixing the liquid waste with polymer to convert the liquid waste to a non-liquid waste:b) contacting the non-liquid waste with sulfur to create a mixture:c) heating the mixture for a time and at a temperature to form homogeneous, chemically stable solid phase: andcompressing the chemically stable solid phase into a final waste monolith wherein the mixture in step c is heated from between approximately 100° C. to approximately 250° C. 3. The method as recited in claim 2 wherein the polymer comprises an elastomer. 4. The method as recited in claim 2 wherein the polymer creates a permanent bond with the waste. 5. The method as recited in claim 2 wherein the solid phase is hardened by the compression. 6. The method as recited in claim 5 wherein the monolith remains leach free for up to about a year while immersed in water. 7. The method as recited in claim 2 wherein the final waste is up to about 10 weight percent aqueous. 8. The method as recited in claim 2 wherein the polymer is an elastomeric selected from the group consisting of styrene block co-polymers, cross linked co-polymers of acrylamide, and combinations thereof. 9. The method as recited in claim 2 wherein the waste comprises up to 100 volume percent of oil. 10. The method as recited in claim 2 wherein the waste comprises radioactive elements selected from the group consisting of cesium, uranium, plutonium, americium, and combinations thereof. 11. The method as recited in claim 2 wherein the weight ratio of polymer to waste ranges from between approximately 1:10 to approximately 10:1. 12. The method as recited in claim 2 wherein the non-aqueous radioactive waste is radiation-contaminated pump oil. 13. A method for immobilizing non-aqueous liquid radioactive waste, the method comprising:a) mixing the liquid waste with polymer to convert the liquid waste to a non-liquid waste;b) contacting the non-liquid waste with sulfur to create a mixture;c) heating the mixture for a time and at a temperature to form homogeneous, chemically stable solid phase; andcompressing the chemically stable solid phase into a final waste monolith wherein the polymers immobilize the nonaqueous liquid. 14. A method for immobilizing liquid radioactive waste containing tritium, the method comprising:a) mixing the liquid waste with polymer to convert the liquid waste to a non-liquid waste;b) contacting the non-liquid waste with a solidifying agent to create a mixture;c) heating the mixture for a time and at a temperature to form homogeneous, chemically stable solid phase; andd) compressing the chemically stable solid phase into a final waste form, wherein the polymer comprises a mixture of styrene block co-polymers and cross linked co-polymers of acrylamides. 15. The method as recited in claim 14 wherein the ratio of styrene block co-polymers and cross linked co-polymers of acrylamides is approximately 9 to 1. 16. The method as recited in claim 14 wherein the heating step occurs in an atmosphere adapted to capture any vaporized tritium. 17. The method as recited in claim 14 wherein radioactive waste is radiation-contaminated pump oil. 18. The method as recited in claim 14 wherein the solidifying agent is an inorganic material comprising kaolin, diatomite, cement, ash, slag, sulfur, selenium and combinations thereof. 19. The method as recited in claim 14 wherein the weight ratio of polymer to waste ranges from between approximately 1:10 to approximately 10:1. 20. The method as recited in claim 14 wherein the mixture is heated from between approximately 100° C. to approximately 250° C.