Background of the Invention
1. Field of the Invention
The present invention relates to a reactor fuel in the form of particles, each particle containing a mixture of plutonium dioxide and uranium dioxide, and to a method for manufacturing such particles.
2. The Prior Art
In traditional pellet manufacture of mixed oxide fuel starting from a mixture of uranium and plutonium oxide powder, there is a risk that plutonium-containing dust will be present in impermissibly high concentrations in working areas and in the surroundings.
Summary of the Invention
This disadvantage is avoided by the invention which is based on the principle of constructing each fuel grain with an outer layer which has such a low plutonium content that dust emanating therefrom does not in itself constitute any danger, and which constitutes a safe canning of material lying inside, the dust from which is harmful.
One further advantage with the particles according to the invention is that after sintering they may be stored for an unlimited time and thereafter be used directly for manufacturing fuel rods by filling into zircaloy tubes. A suitable enrichment according to the specification adequate for each fuel delivery can be obtained by mixing a few available particle types with different enrichments. Because of the small number of manufacturing operations, this manufacture may be performed independently of a successively increasing buildup of the content of gamma-active americium 241, as opposed to the case when plutonium dioxide powder is the starting material. Further the alpha activity does not induce changes in the applicability of the particles for a continued manufacture of fuel after storing in the same way as is true of plutonium dioxide powder, because the alpha radiation is completely absorbed in the interior of the particles and does not affect the surface. Because of this it is practical, immediately in the reprocessing plant, to convert the plutonium to particles of the type described, before it is put in stock. This will also cause a radical reduction of the otherwise inconvenient amount of solid alpha active waste material which is the result of the manufacture of mixed oxide fuel according to the present conventional methods.
A mixed oxide particle according to the invention has a diameter of from 0.2 to 2 mm and a surface layer of UO.sub.2 with a thickness of at least 0.05 mm and a high degree of purity, that is, with a plutonium content per volume unit of at the most 15% of the average plutonium content per volume unit of the particle.
The invention also relates to a method for manufacturing a mixed fuel particle which is formed with an outer, practically plutonium-free layer, more particularly according to the so-called "sol-gel" principle. This is known, among other things, from the publication "Sol-Gel Processes for Ceramic Nuclear Fuels," published by the International Atomic Energy Agency, Vienna, 1968. The present invention is a further development of said known process, and makes it possible to manufacture mixed oxide fuel grains with materials varying in layers, in particular with a plutonium-free surface layer.
According to the invention, the particles are formed in a nozzle having inner and outer parts by pumping water emulsion of uranium dioxide through the central part, then pumping water emulsion of plutonium dioxide through the outer nozzle to surround the uranium dioxide, then pumping a water emulsion of uranium dioxide through an outer nozzle to cover the plutonium dioxide and then pumping uranium dioxide through the inner nozzle to complete the enclosure of the plutonium dioxide.
Brief Description of the Drawings
One example of the method for manufacturing particles will be explained in the following with reference to the accompanying drawings, in which
FIG. 1 shows a system for carrying out the method, whereas
FIGS. 2 to 6 show different stages in the manufacturing process.
FIG. 7 shows on an enlarged scale a detail of FIG. 1.
Description of the Preferred Embodiments
In the drawings, 1 and 1' designate containers for uranium oxide UO.sub.2, which has low radioactivity, and 2 designates a container for plutonium dioxide, PuO.sub.2 which, like UO.sub.2, is supplied emulsified in water in the form of a so-called "sol." Although the chemical conditions of uranium and plutonium in the respective emulsions do not exactly correspond to the respective dioxides, these designations are used in the following.
3 and 4 are tanks which are filled with a hydrophobic solvent, for example paraffin, and 5, 6, 7, 8 and 9 designate pulse-controlled pumps having small stroke volumes. They are driven by electric motors, not shown in the drawing, which are supplied with electric pulses according to a permanent program which is repeated for each new fuel grain to be formed.
The annular nozzle 10 surrounds a tube with a central nozzle 11 and extends below the surface of a water-absorbing liquid in vessel 12. A large number of nozzles are connected to each dosing pump. The pipes and nozzles are made of water-repellent material, with the exception of the very tip of nozzle 11, which is made of hydrophilic material, for example glass.
At each stroke of the pump either paraffin, UO.sub.2 or PuO.sub.2 is driven through any of the nozzles 10 and 11. The finished droplets leave the nozzle 11 and sink deeper down into the vessel 12 which is filled with a strongly water-absorbing liquid, for example 2-ethyl hexanol. The jelly-like particles which are then formed are collected on a grid 13, from which they are transported to a drying and sintering plant to finally acquire the shape of solid, relatively hard fuel grains. Paraffin and ethyl hexanol are separated in a suitable plant, for example by means of distillation, and are returned to the process.
FIG. 7 shows in detail the resulting effect of the two pumps 7 and 9. In the capillary tube 14 strings of paraffin and of UO.sub.2 solution alternate on their way towards the capillary nozzle 11. In a similar way alternate strings of alternate paraffin and PuO.sub.2 solution follow after each other in the capillary tube 15.
As is clear from FIGS. 2 and 3, the particle formation is started by supplying UO.sub.2 to the nozzle 11 and pressing it out through this nozzle, so that a small primary droplet 16 of UO.sub.2 is formed. Thereafter a string 17 of PuO.sub.2 comes through the nozzle 10 and covers the main part of the surface of the primary droplet 16 with a layer 18 of PuO.sub.2, as shown in FIG. 4. After an interval with paraffin, a string of UO.sub.2 solution then comes from container 1' through nozzle 10 and forms a UO.sub.2 layer 19, which surrounds practically the whole PuO.sub.2 layer 18. A complete enclosure is achieved by a final supply of UO.sub.2 solution through the nozzle 11, the particle then being repelled from the nozzle. As is indicated in the drawing, the particle has a spherical or almost spherical shape.
FIG. 6 shows at the bottom the finished particle on its way towards the collecting grid 13.
The collected particles are dried and thereafter subjected, in a manner known per se, to a heating to such a high temperature that sintering takes place within each particle.
The proposed process is only one of several feasible processes in order to form the mixed oxide particle with a plutonium oxide-free surface layer.