Patent Number: 042319765
Section: claims

1. A process for the production of a plutonium-uranium ceramic fuel wherein green pellets are formed by pressing from: (i) a mixture of (a) an oxide, finely-divided carbon-containing oxide, carbide, nitride, oxycarbide, or carbonitride of plutonium, in the form of microspheres obtained by a wet chemical process, and (b) a like compound of uranium in a form selected from such microspheres and fine-grained to pulverulent materials; or  (ii) a like compound of a plutonium-uranium solid solution of which at least 1% is plutonium, in the form of microspheres obtained by a wet chemical process, alone or in admixture with a material selected from the said plutonium-compound microspheres, the said uranium-compound microspheres, and the said fine-grained to pulverulent materials,  (a) mixing together a plutonium-containing compound and a uranium-containing compound, said plutonium-containing compound being in the form of microspheres produced by a wet chemical process and being selected from the group consisting of an oxide, a carbon-containing oxide, a carbide, a nitride, an oxycarbide, and a carbonitride; and said uranium-containing compound being in the form of either microspheres or else a fine-grained to pulverulent form of a uranium compound selected from the group consisting of an oxide, a carbon-containing oxide, a carbide, a nitride, an oxycarbide, and a carbonitride,  (b) pressing the mixture formed in step (a) to form green pellets, and  (c) heat treating the green pellets in step (b) to form a plutonium-uranium ceramic fuel.  (a) forming microspheres of a plutonium-uranium solid solution by a wet chemical process, said plutonium-uranium solid solution containing at least 1% plutonium, said plutonium-uranium solid solution containing plutonium compounds selected from the group consisting of an oxide, a carbon-containing oxide, a carbide, a nitride, an oxycarbide, and a carbonitride, and said plutonium-uranium solid solution containing uranium compounds selected from the group consisting of an oxide, a carbon-containing oxide, a carbide, a nitride, an oxycarbide, and a carbonitride,  (b) pressing the microspheres in step (a) to form green pellets, and  (c) heat treating the green pellets in step (b) to form a plutonium-uranium ceramic fuel.  (a) mixing together (i) microspheres obtained from a wet chemical process of a plutonium-uranium solid solution, said solid solution containing at least 1% plutonium, said plutonium-uranium solid solution containing plutonium compounds selected from the group consisting of an oxide, a carbon-containing oxide, a carbide, a nitride, an oxycarbide, and a carbonitride, and said plutonium-uranium solid solution containing uranium compounds selected from the group consisting of an oxide, a carbon-containing oxide, a carbide, a nitride, an oxycarbide, and a carbonitride, (ii) microspheres of plutonium-containing compounds produced by a wet chemical process, said plutonium-containing compounds selected from the group consisting of an oxide, a carbon-containing oxide, a carbide, a nitride, an oxycarbide, and a carbonitride, and (iii) a uranium-containing compound either in microsphere form or else a fine-grained to pulverulent form, said uranium-containing compound selected from the group consisting of an oxide, a carbon-containing oxide, a carbide, a nitride, an oxycarbide, and a carbonitride,  (b) pressing the mixture formed in step (a) to form green pellets, and  (c) heat treating the green pellets in step (b) to form a plutonium-uranium ceramic fuel. 2. A process according to claim 1 wherein, for the production of sintered pellets with a specified plutonium to heavy metal ratio, xerogel microspheres of a solid solution of uranium plutonium obtained in a gelation process are pressed to green pellets with the same plutonium to heavy metal ratio and the green pellets are calcined at a certain temperature and sintered at a higher temperature in the course of a heat treatment. 3. A process according to claim 2, wherein xerogel microspheres produced by a gel-precipitation process are used for the production of uranium-plutonium mixed oxide pellets. 4. A process according to claim 3, wherein the xerogel microspheres of plutonium and uranium have mixed or uniform diameter of 20 to 100 .mu.m. 5. A process according to claim 2, wherein the green pellets are calcined in a reducing gas of 80% argon and 20% hydrogen at 500.degree. C. and subsequently are sintered in an oven at 1400.degree. to 1600.degree. C. 6. A process according to claim 5, wherein the green pellets are sintered to 95-98% of the theoretical density. 7. A process according to claim 2, wherein xerogel microspheres of uranium-plutonium made according to the "EIR sol-gel process" are used for the production of uranium-plutonium mixed carbide pellets, wherein the microspheres contain about 12 weight parts, related to the total weight, of finely divided carbon-black and have diameters lying in the range of 20 to 200 .mu.m. 8. A process according to claim 7, wherein the green pellets are calcined in flowing gas of 20% hydrogen and 80% argon at about 500.degree. C. and then are subjected to a heat treatment in flowing argon of 1700.degree. to 1800.degree. C., during which a carbon reduction takes place and the pellets are sintered. 9. A process according to claim 8, wherein the pellets are sintered to 95% of the theoretical density. 10. A process according to claim 1, wherein for the production of sintered pellets with a specified plutonium to heavy metal ratio, a xerogel microsphere of uranium obtained in a gelation process or fine-grained to pulverulent uranium material is used in a weight ratio determined by the plutonium to heavy metal ratio and are mixed with xerogel microspheres of plutonium obtained in a gelation process, the uranium particles and the plutonium microspheres having at least approximately the same size distribution and about the same mean diameter, and wherein the particle mixture is pressed to green pellets, and in the course of a heat treatment the green pellets are calcined at a specified temperature and sintered at a higher temperature. 11. A process according to claim 10, wherein the uranium microspheres or the fine-grained to pulverulent material and the plutonium microspheres pressed to green pellets have particle diameters lying in the range of 5 to 25 .mu.m and a mean diameter of 10 to 15 .mu.m. 12. A process according to claim 10, wherein uranium xerogel microspheres made by the "Julich H-Process" and plutonium xerogel microspheres produced by an "EIR Sol-Gel Process" are used for the production of uranium-plutonium mixed oxide pellets, particularly for LW reactors. 13. A process according to claim 12, wherein the green pellets are calcined in a reducing gas of 80% argon and 20% hydrogen at about 500.degree. C. and then sintered in argon at 1400.degree. to 1600.degree. C. 14. A process according to claim 13, wherein the pellets are sintered to 95-98% of the theoretical density. 15. A process according to claim 1, wherein the calcined xerogel microspheres of plutonium obtained in a gelation process and the calcined xerogel microspheres of uranium obtained in a gelation process or a corresponding fine-grained to pulverulent uranium material are mixed together in a certain weight ratio, the uranium particles and the plutonium microspheres having at least approximately the same size distribution and about the same mean diameter, and wherein the mixture is pressed to green pellets and the green pellets are sintered at a higher temperature. 16. A process according to claim 15, wherein the uranium particles and the plutonium microspheres have a diameter in the range of 5 to 25 .mu.m. 17. A process according to claim 15, wherein uranium oxide microspheres produced according to an "ORNL Sol-Gel Process" and plutonium oxide microspheres produced by a PuO.sub.2 Sol-gel process are used for the production of uranium-plutonium mixed oxide pellets, particularly for FB reactors. 18. A process according to claim 15, wherein the green pellets are sintered in a flowing gas of argon and 4% hydrogen at 1200.degree. to 1300.degree. C. 19. A process according to claim 18, wherein the pellets are sintered to 95-98% of the theoretical density. 20. A process according to claim 1, wherein the plutonium xerogel microspheres obtained in a gelation process are calcined at a specified temperature and the thus obtained plutonium oxide microspheres are subjected to reaction sintering at a higher temperature; that the sintered plutonium microspheres are mixed with microspheres or uranium with a fine-grained to pulverulent uranium material, both kinds of particles having at least approximately the same size distribution and about the same mean diameter, and wherein green pellets are pressed from the mixture and the green pellets are subjected to final sintering. 21. A process according to claim 20, wherein the uranium xerogel microspheres obtained in a gelation process are calcined at a specified temperature and the thus obtained uranium microspheres are subjected to reaction sintering at a higher temperature and the sintered uranium oxide microspheres are mixed with the reaction-sintered plutonium microspheres. 22. A process according to claim 20, wherein the reaction-sintered plutonium microspheres are mixed with a fine-grained to pulverulent uranium material which is calcined and/or reaction sintered. 23. A low-dust process for the production of a homogeneous plutonium-uranium ceramic fuel which comprises the steps of 24. The low-dust process in accordance with claim 23 wherein said uranium-containing compound is in the form of microspheres, and wherein both said plutonium-containing compound microspheres and said uranium-containing compound microspheres are separately calcined prior to being mixed together in said step (a). 25. The low-dust process in accordance with claim 24 wherein said uranium-containing compound microspheres include finely divided carbon. 26. The low-dust process in accordance with claim 25 wherein prior to the mixing together of said plutonium-containing compound microspheres and subsequent to the separate calcinations of said microspheres, said microspheres are separately presintered. 27. The low-dust process in accordance with claim 23 wherein said uranium-containing compound is in the form of a fine-grained to pulverulent compound, and wherein said plutonium-containing compound is calcined prior to being mixed together with said uranium-containing compound in step (a). 28. The low-dust process in accordance with claim 23 wherein said uranium-containing compound is in the form of a fine-grained to pulverulent compound, and wherein said plutonium-containing compound microspheres are pre-sintered prior to being mixed together with said uranium-containing compound in said step (a). 29. The low dust process in accordance with claim 28 wherein said uranium-containing compound is in the form of a fine-grained to pulverulent compound is pre-sintered prior to being mixed with said pre-sintered plutonium-containing compound. 30. A low-dust process for the production of a homogeneous plutonium-uranium ceramic fuel which comprises the steps of 31. A low-dust process for the production of a homogeneous plutonium-uranium ceramic fuel which comprises the steps of