Patent Number: 053486897
Section: claims

1. A process for destroying alkali metal and alkaline earth metal hazardous waste and converting it into non-hazardous salt which comprises feeding said alkali metal or alkaline earth metal containing hazardous waste into a molten salt bath containing a molten salt selected from the group consisting of an alkali metal carbonate, an alkali metal halide, an alkaline earth halide, and mixtures thereof,  feeding a mixture of carbon dioxide and oxygen into said molten salt bath, the proportions of carbon dioxide and oxygen being at least sufficient to react stoichiometrically with the alkali metal or alkaline earth metal in said waste, and  reacting said alkali metal or said alkaline earth metal with said carbon dioxide and oxygen in said molten salt bath at a temperature above the melting point of the salt in said molten salt bath, and converting said alkali metal or said alkaline earth metal into a non-hazardous carbonate salt in said bath.  introducing said sodium-containing hazardous waste into a molten sodium carbonate bath,  introducing a mixture of carbon dioxide and oxygen into said molten sodium carbonate bath, the proportions of carbon dioxide and oxygen being at least 10% in excess of the stoichiometric amount required for reaction with said sodium in said waste,  reacting said sodium in said waste with said carbon dioxide and oxygen in said molten sodium carbonate bath at temperature of between about 800.degree. C. and about 900.degree. C,. and converting said sodium into sodium carbonate in said bath.  introducing said sodium-containing hazardous waste into a molten salt bath, said salt bath consisting of a mixture of sodium carbonate and a member selected from the group consisting of alkali metal chloride and alkaline earth metal chloride,  introducing a mixture of carbon dioxide and oxygen into said molten salt bath, the proportions of carbon dioxide and oxygen being at least 10% in excess of the stoichiometric amount required for reaction with said sodium in said waste,  reacting said sodium in said waste with said carbon dioxide and oxygen in said molten salt bath at a temperature between about 600.degree. C. and about 800.degree. C., and converting said sodium into sodium carbonate in said bath.  feeding said alkali metal or alkaline earth metal containing hazardous waste into a molten salt bath containing a molten salt consisting of a mixture of sodium carbonate and a lower melting point salt consisting of a mixture of alkali metal chlorides and alkaline earth metal chlorides, said molten salt bath temperature ranging from about 600.degree. C. to about 800.degree. C.,  feeding a mixture of carbon dioxide and oxygen into said molten salt bath, the proportions of carbon dioxide and oxygen being at least sufficient to react stoichiometrically with the alkali metal or alkaline earth metal in said waste, and  reacting said alkali metal or said alkaline earth metal with said carbon dioxide and oxygen in said molten salt bath at a temperature above the melting point of the salt in said molten salt bath, and converting said alkali metal or said alkaline earth metal into a non-hazardous carbonate salt in said bath.  feeding said alkali metal or alkaline earth metal containing hazardous waste into a molten salt bath consisting of a mixture of sodium carbonate and a lower melting point salt selected from the group consisting of alkali metal halides, alkaline earth metal halides, and mixtures thereof, said molten salt bath temperature ranging from about 600.degree. C. to about 800.degree. C.,  feeding a mixture of carbon dioxide and oxygen into said molten salt bath, the proportions of carbon dioxide and oxygen being at least sufficient to react stoichiometrically with the alkali metal or alkaline earth metal in said waste, and  reacting said alkali metal or said alkaline earth metal with said carbon dioxide and oxygen in said molten salt bath at a temperature above the melting point of the salt in said molten salt bath, and converting said alkali metal or said alkaline earth metal into a non-hazardous carbonate salt in said bath,  said lower melting point salt being maintained by sparging chlorine or chlorinated hydrocarbon into said molten salt bath to convert carbonate therein to chlorides.  feeding said sodium containing hazardous waste into a molten salt bath consisting of a mixture of two or more salts selected from the group consisting of NaCl, KCl and CaCl.sub.2,  feeding a mixture of carbon dioxide and oxygen into said molten salt bath, the proportions of carbon dioxide and oxygen being at least sufficient to react stoichiometrically with the sodium in said waste, and  reacting said sodium with said carbon dioxide and oxygen in said molten salt bath at a temperature above the melting point of the salt in said molten salt bath, and converting said sodium into non-hazardous sodium carbonate in said bath.  feeding said alkali metal or alkaline earth metal containing hazardous waste into a molten salt bath containing a molten salt consisting of a eutectic of about 50% Na.sub.2 CO.sub.3 and about 50% NaCl, by weight,  feeding a mixture of carbon dioxide and oxygen into said molten salt bath, the proportions of carbon dioxide and oxygen being at least sufficient to react stoichiometrically with the alkali metal or alkaline earth metal in said waste, and  reacting said alkali metal or said alkaline earth metal with said carbon dioxide and oxygen in said molten salt bath at a temperature above the melting point of the salt in said molten salt bath, and converting said alkali metal or said alkaline earth metal into a non-hazardous carbonate salt in said bath. 2. The process of claim 1, and including adding a member selected from the group consisting of sulfate, phosphate and nitrate to said molten salt to lower the melting point of the salt. 3. The process of claim 1, wherein the temperature of said molten bath ranges from about 200.degree. C. to about 900.degree. C. 4. The process of claim 1, wherein said molten salt bath consists essentially of sodium carbonate and molten salt bath temperature ranges from about 600.degree. C. to about 900.degree. C. 5. The process of claim 3, wherein said waste contains alkali metal, and said alkali metal is sodium, and said sodium is converted to sodium carbonate in said molten salt bath. 6. The process of claim 1, wherein said molten salt bath consists of a mixture of sodium carbonate and a lower melting point salt selected from the group consisting of alkali metal halides, alkaline earth metal halides, and mixtures thereof, and said molten salt bath temperature ranges from about 600.degree. C. to about 800.degree. C. 7. The process of claim 1, wherein the proportions of carbon dioxide and oxygen are at least 10% in excess of the stoichiometric amount required for reaction with the alkali metal or alkaline earth metal in said bath. 8. A process for destroying sodium in hazardous waste and converting it into non-hazardous sodium carbonate which comprises 9. A process for destroying sodium in hazardous waste and converting it into non-hazardous sodium carbonate which comprises 10. The process of claim 9, wherein said member is a mixture of two or more salts selected from the group consisting of NaCl, and KCl and CaCl.sub.2. 11. The process of claim 9, wherein said salt bath consists of a eutectic alkali carbonate mixture consisting of 50% Na.sub.2 CO.sub.3 and 50% K.sub.2 CO.sub.3, by weight and a mixture of two or more salts selected from the group consisting of NaCl, KCl and CaCl.sub.2. 12. A process for destroying alkali metal and alkaline earth metal hazardous waste and converting it into non-hazardous salt which comprises 13. The process of claim 12, wherein said waste contains alkali metal, and said alkali metal is sodium, and said lower melting point salt consists of a mixture of two or more salts selected from the group consisting of NaCl, KCl and CaCl.sub.2. 14. A process for destroying alkali metal and alkaline earth metal hazardous waste and converting it into non-hazardous salt which comprises 15. The process of claim 1, wherein said molten salt bath consists of a member selected from the group consisting of an alkali metal halide, an alkaline earth halide, and mixtures thereof. 16. The process of claim 1, wherein said molten salt is a eutectic alkali carbonate mixture consisting of 50% Na.sub.2 CO.sub.3 and 50% K.sub.2 CO.sub.3, by weight. 17. A process for destroying sodium in sodium-containing hazardous waste and converting it into non-hazardous salt which comprises 18. A process for destroying alkali metal and alkaline earth metal hazardous waste and converting it into non-hazardous salt which comprises