Patent Number: 051397099
Section: claims

1. A process for the conversion of UF.sub.6 to UO.sub.2 comprising the steps of (a) pyrohydrolyzing gaseous UF.sub.6 with steam in a reactor to prepare UO.sub.2 F.sub.2 powder;  (b) dissolving the UO.sub.2 F.sub.2 powder in water to form an aqueous UO.sub.2 F.sub.2 solution;  (c) atomizing the aqueous UO.sub.2 F.sub.2 solution and contacting the atomized solution with an ammonia-containing gas stream to produce wet ADU particles;  (d) drying and calcining the ADU particles to obtain a calcined powder; and  (e) reducing the calcined powder to UO.sub.2 with a hydrogen gas or a hydrogen-steam mixture.  (a) dissolving the uranyl compound in water to obtain an aqueous solution of the uranyl compound;  (b) atomizing the aqueous solution and contacting the atomized solution with an ammonia-containing gas stream to produce wet ADU particles;  (c) drying and calcining the ADU particles to obtain a calcined powder; and  (d) reducing the calcined powder to UO.sub.2 with a hydrogen gas or a hydrogen-steam mixture. 2. A process for the conversion of a uranyl compound to UO.sub.2 comprising the steps of 3. The process according to claim 2, in which gadolinium nitrate is also dissolved in the aqueous solution of the uranyl compound obtained in step (a) to produce a Gd.sub.2 O.sub.3 -UO.sub.2 powder in step (d). 4. The process according to claim 1, in which the concentration of UO.sub.2 F.sub.2 in the aqueous UO.sub.2 F.sub.2 solution used for atomizing in step (c) is below the saturation concentration of UO.sub.2 F.sub.2 in the solution. 5. The process according to claim 1, in which the ammonia-containing gas used for the preparation of ADU in step (c) is a single component gas, or a gas mixture containing ammonia gas. 6. The process according to claim 1, in which the temperature used for drying and calcining in step (d) is below 750.degree. C. 7. The process according to claim 1, in which the reduction temperature used in step (e) is below 850.degree. C. 8. The process according to claim 4, in which the temperature of the aqueous UO.sub.2 F.sub.2 solution is below its boiling point. 9. The process according to claim 5, in which the operation temperature used in the preparation of ADU is below 200.degree. C. 10. The process according to claim 9, in which the pressure of the ammonia-containing gas stream used is below 10 atm. 11. The process according to claim 2, in which the concentration of the uranyl compound in the aqueous solution used for atomizing in step (b) is below the saturation concentration of the uranyl compound in the solution. 12. The process according to claim 2, in which ammonia-containing gas used for the preparation of ADU in step (b) is a single componet gas, or a gas mixture containing ammonia gas. 13. The process according to claim 2, in which the temperature used for drying and calcining in step (c) is below 750.degree. C. 14. The process according to claim 2, in which the reduction temperature used in step (d) is below 850.degree. C. 15. The process according to claim 11, in which the temperature of the aqueous solution of the uranyl compound is below its boiling point. 16. The process according to claim 12, in which the temperature used in the preparation of ADU is below 200.degree. C. 17. The process according to claim 16, in which the pressure of the ammonia-containing gas stream used is below 10 atm. 18. The process according to claim 3, in which the weight ratio of uranium to the total of uranium and gadolinium in the Gd.sub.2 O.sub.3 -UO.sub.2 powder is larger than 0.7. 19. The process according to claim 18, in which the concentration of the uranyl compound and gadolinium in the aqueous solution used for atomizing in step (b) is below the saturation concentration of the uranyl compound and gadolinium in the solution. 20. The process according to claim 3, in which ammonia-containing gas used for ammoniation in step (b) is a single component gas, or a gas mixture containing ammonia gas. 21. The process according to claim 3, in which the temperature used for drying and calcining in step (c) is below 750.degree. C. 22. The process according to claim 3, in which the reduction temperature used in step (d) is below 900.degree. C. 23. The process according to claim 19, in which the temperature of the aqueous solution used for ammoniation is below its boiling point. 24. The process according to claim 20, in which the operation temperature of ammoniation is below 200.degree. C. 25. The process according to claim 20, in which the pressure of the ammonia-containing gas stream used is below 10 atm.