Patent Number: 045591709
Section: claims

1. A process for reducing the volume of a bead ion exchange resin waste, said beads having a mean diameter of about 500 to 800 microns and said waste being contaminated with a member selected from the group consisting of the radionuclides Cs.sup.134, Cs.sup.137, Co.sup.58, Co.sup.60, I.sup.129, and mixtures thereof, said bead ion exchange resin waste containing water on the surface of ion exchange resin beads and water inside said ion exchange resin beads, which consists essentially of: introducing said bead ion exchange resin waste in the form of a finely atomized spray into a spray drying zone and contacting it with a hot gas stream within said zone, said gas stream having a temperature in the range of about 200.degree. to 450.degree. C. and sufficient to vaporize the water on the surface of said ion exchange resin beads and to remove the water inside said ion exchange resin beads, but insufficient to oxidize or combust said bead ion exchange resin waste or volatilize said radionuclides;  maintaining said bead ion exchange resin waste in said spray drying zone for a residence time of about 3 to 12 seconds;  removing from said zone dry ion exchange resin beads containing said radionuclides and containing substantially no water, and a gaseous nonradioactive product comprising water vapor, said gaseous product containing substantially no oxidation or combustion products of said bead ion exchange resin waste, the ratio of the volume of said bead ion exchange resin waste to said dry ion exchange resin beads being in the range of about 1.5:1 to 3:1; and  separating said dry ion exchange resin beads from said gaseous nonradioactive product.  introducing said bead ion exchange resin waste in the form of a finely atomized spray into a spray drying zone and contacting it with a hot gas stream, said stream having a temperature in the range of about 200.degree. to 450.degree. C. and sufficient to vaporize the water on the surface of said ion exchange resin beads and to remove the water inside said ion exchange resin beads, but insufficient to oxidize or combust said bead ion exchange resin waste or volatilize said radionuclides;  maintaining said bead ion exchange resin waste in said spray drying zone for a residence time of about 3 to 12 seconds;  removing from said zone dry ion exchange resin beads containing said radionuclides and containing substantially no water, and a gaseous nonradioactive product comprising water vapor, said gaseous product containing substantially no oxidation or combustion products of said bead ion exchange resin waste, the ratio of the volume of said bead ion exchange resin waste to said dry ion exchange resin beads being in the range of about 1.5:1 to 3:1;  separating said dry ion exchange resion beads from said gaseous nonradioactive product; and  mixing said dry ion exchange resin beads with a solid matrix-forming composition comprising a copolymer of styrene and vinyl ester;  thereby forming a solid monolith containing said dry ion exchange resin beads and having a radionuclide leachability below about 10.sup.-2 g/cm.sup.2 /day. 2. A process according to claim 1 wherein said bead ion exchange resin waste comprises an aqueous slurry. 3. A process according to claim 1 wherein said temperature is in the range of about 300.degree. to 350.degree. C. 4. A process according to claim 3 wherein said residence time is about 3 to 6 seconds. 5. A process according to claim 1 wherein said temperature is in the range of about 275.degree. to 325.degree. C. and said residence time is about 5 to 10 seconds. 6. A process according to claim 1 wherein said hot gas is produced by burning a fuel in an excess of an oxygen-containing gas. 7. A process according to claim 1 wherein said hot gas is produced by burning fuel oil in an excess of an oxygen-containing gas. 8. A process according to claim 1 wherein said dry ion exchange resin beads are separated from said gaseous nonradioactive product by passing said mixture of dry beads and gaseous product through a dry cyclone. 9. A process according to claim 1 wherein said hot gas is produced by means of an electrically heated gas heater. 10. A process for disposing of a bead ion exchange resin waste, said beads having a mean diameter of about 500 to 800 microns and said waste being contaminated with a member selected from the group consisting of the radionuclides Cs.sup.134, Cs.sup.137, Co.sup.58, Co.sup.60, I.sup.129, and mixtures thereof, said bead ion exchange resin waste containing water on the surface of ion exchange resin beads and water inside said ion exchange resion beads, which consists essentially of: 11. A process according to claim 10 wherein said leachability is less than about 10.sup.-4 g/cm.sup.2 /day. 12. A process according to claim 10 wherein said dry ion exchange resin beads are mixed with said solid matrix-forming composition in a ratio of about 0.35:1 to 4:1. 13. A process according to claim 10 wherein said dry ion exchange resin beads are mixed with said solid matrix-forming composition in a ratio of about 1.5:1 to 2.5:1.