Thermal conversion of wastes

Claim 2

A process for converting a strong cation exchange resin contaminated with a radioactive substance into a non-radioactive gas substantially free of oxides of sulfur and a radioactive inorganic ash which comprises: introducing an aqueous slurry comprising said strong cation exchange resin and an alkaline material selected from the group consisting of alkali and alkaline earth metal hydroxides and carbonates, in the form of a finely atomized spray, into the top of a zone heated, by means of a hot gas produced externally of said zone and introduced into the top of said zone, to a temperature sufficient to convert said strong cation exchange resin, by contact with said hot gas, into a mixture of products comprising a non-radioactive gas substantially free of oxides of sulfur and a radioactive inorganic ash; removing said mixture of products from the bottom of said zone; and separating said radioactive inorganic ash from said mixture of products, the ratio of the volume of said strong cation exchange resin to the volume of said radioactive inorganic ash being in the range of about 20:1 to 70:1.

Claim 3

A process according to claim 1 wherein said alkaline material is added to the aqueous slurry of said ion exchange resin in a ratio by weight of about 1:10 to 10:1 based on said ion exchange resin whereby said oxides of sulfur are substantially completely removed from said mixture of products.

Claim 4

A process for converting a strong anion exchange resin contaminated with a radioactive substance into a non-radioactive gas substantially free of oxides of nitrogen and a radioactive inorganic ash which comprises: introducing an aqueous slurry of said strong anion exchange resin in the form of a finely atomized spray into the top of a zone heated, by means of a hot gas produced externally of said zone and introduced into the top of said zone, to a temperature sufficient to convert said strong anion exchange resin, by contact with said hot gas, into a mixture of products comprising a non-radioactive gas containing oxides of nirogen and a radioactive inorganic ash; removing said mixture of products from the bottom of said zone; injecting a base selected from the group consisting of NH 3 , CH 3 NH 2 and (CH 3 ) 2 NH into said non-radioactive gas downstream of said zone to produce a non-radioactive gas substantially free of oxides of nitrogen and separating said radioactive inorganic ash, the ratio of the volume of said strong anion exchange resin to the volume of said radioactive inorganic ash being in the range of about 20:1 to 70:1.

Claim 5

A process for converting a strong anion exchange resin contaminated with a radioactive substance into a non-radioactive gas substantially free of oxides of nitrogen and a radioactive inorganic ash which comprises: introducing an aqueous slurry of said strong anion exchange resin in the form of a finely atomized spray into the top of a zone heated, by means of a hot gas produced externally of said zone and introduced into the top of said zone, to a temperature sufficient to convert said strong anion exchange resin, by contact with said hot gas, into a mixture of products comprising a non-radioactive gas containing oxides of nirogen and a radioactive inorganic ash; removing said mixture of products from the bottom of said zone; injecting a base selected from the group consisting of NH 3 , CH 3 NH 2 and (CH 3 ) 2 NH into said non-radioactive gas downstream of said zone to produce a non-radioactive gas substantially free of oxides of nitrogen and separating said radioactive inorganic ash, the ratio of the volume of said strong anion exchange resin to the volume of said radioactive inorganic ash being in the range of about 20:1 to 70:1.

Claim 6

A process according to claim 3 wherein said base is injected in a ratio by weight of about 1:10 to 10:1 based on said ion exchange resin, whereby said oxides of nitrogen are substantially completely removed from said mixture of products.