Patent Number: 043671845
Section: description

DETAILED DESCRIPTION In the past nuclear reactor fuels containing highly enriched uranium (as much as 93% U.sup.235) have been used, but as mentioned hereinbefore such fuels are undesirable because the uranium can easily be used in atomic weapons. The use of uranium of lower enrichment for reactor fuel involves manufacturing problems that are difficult to solve. For example, fuel microspheres made of highly enriched uranium may have a low density, whereas microspheres made of uranium containing less U.sup.235 must have a high density. In addition, the form of the uranium in reactor fuel microspheres is of crucial importance. Microspheres consisting of UO.sub.2 alone are unacceptable because under operational conditions in a reactor this material adversely affects a pyrolytic carbon coating that is applied to the microspheres for a purpose not important to an understanding of this invention. A composition consisting of UC.sub.2 and UO.sub.2 can be used to form dense reactor fuel microspheres that are not easily processed to supply fissile material for weapons. However, such UC.sub.2 /UO.sub.2 microspheres must contain at least 15 mole percent UO.sub.2 to prevent attack by fission products generated in the microspheres upon a SiC coating that is applied to the latter in addition to the previously mentioned carbon coating. An optimal combination of UO.sub.2 and UC.sub.2 prevents deterioration of both of the coatings. In accordance with this invention, microspheres having the desired composition of UO.sub.2 and UC.sub.2 and a high density are manufactured by a sintering process involving carbothermic reduction of UO.sub.2 to UC.sub.2 in an atmosphere consisting of CO and an inert gas. It is an important advantage of the invention that this manufacturing process occurs in such a way that neither uranium oxycarbide or uranium monocarbide is included in the fuel composition, since each of these compounds can cause damage, under operational conditions in a reactor, to the aforementioned pyrolytic carbon coating applied to fuel microspheres. The preferred process of this invention can best be understood by reference to FIGS. 1 and 2 which illustrate the phase relationships of the U-C-O system between 1300.degree. and 1750.degree. C., the components in some of the phase regions of the diagram not being identified because they are not involved in the process. For use in a high temperature, gas-cooled reactor a composition consisting of 1 to 30 mole percent UC.sub.2 is desirable. A percentage of UC.sub.2 as high as 55 would be acceptable, but the required density of microspheres is difficult to achieve for UC.sub.2 concentrations greater than 30%. The desired UC.sub.2 -UO.sub.2 composition range is located along the line joining UC.sub.2 and UO.sub.2 on the phase diagram and is represented by a narrow rectangular area at the lower portion of this tie line. The UC.sub.2 phase actually contains a minor amount of oxygen and has a composition of UC.sub.1.83 O.sub.0.075. Three phase fields are involved in a carbothermic reduction process which occurs in the portion of the diagram where the desired UC.sub.2 /UO.sub.2 composition range is located. One compatibility triangle includes the phases UO.sub.2, UC.sub.2, and carbon, the UC.sub.2 containing a minor amount of oxygen as stated above. A composition within this triangle would not be acceptable for use as fuel in a high temperature, gas-cooled reactor because of the free carbon therein, which would drastically reduce the density of sintered microspheres formed of the composition. A second compatibility triangle of interest includes the previously mentioned UC.sub.2 and UO.sub.2 phases plus uranium oxycarbide, the latter being represented as UC.sub.x O.sub.y. A composition within this triangle is unacceptable because of the presence of UC.sub.x O.sub.y, since, as stated earlier, uranium oxycarbide can cause damage to the pyrolytic carbon coating applied to fuel microspheres. The last compatibility triangle that must be considered in connection with the invention is the region that includes UC.sub.x O.sub.y and UO.sub.2. A microsphere composition in this two-phase region is again unacceptable because of the presence of UC.sub.x O.sub.y. The reaction occurring during the carbothermic reduction process involved in this invention is represented by the following equation: EQU UO.sub.2 +4C=UC.sub.2 +2CO The composition after calcination of microspheres usable in the carbothermic reduction process of the invention can include 45 to 97 mole percent UO.sub.2 and 3 to 55 mole percent free carbon. This range is located along the line joining C and UO.sub.2 on the phase diagram and is represented by a bracket at the lower portion of the tie line. Microspheres having a UO.sub.2 --C composition within the stated range (which will be referred to hereinafter as precursor microspheres) have been formed by a process similar to the process described in an article titled "The KEMA U(VI) Process for the Production of UO.sub.2 Microspheres," which was published by J. Kanij, A. Noothout and O. Votocek in May, 1973, in connection with a symposium relating to sol-gel processes for forming nuclear fuel. The solutions used in the above-identified KEMA process can be used to form precursor microspheres, which by means of this invention can be converted into nuclear fuel microspheres usable in a high temperature, gas-cooled reactor, by adding carbon black to the KEMA components. However, the steps that have been used to form precursor microspheres usable in the process of this invention are described in the following paragraph only as an example of a suitable method for making the precursor microspheres, and other means can optionally be used to produce microspheres within the UO.sub.2 -C range stated above. To obtain precursor microspheres, 0.2 gram of a dispersing agent (e.g., Marasperse CB or Marasperse CBOS-6) can be dissolved in 171 ml of a 3.12 molar solution of hexamethylenetetramine and water and then 5.37 grams of carbon black having an average particle size of 24.times.10.sup.-3 .mu.m and a surface area of 138 m.sup.2 /g (e.g., carbon black available from Cabot Corporation under the name Black Pearls L) is added while the solution is being agitated by a Branson ultrasonic vibrator, the temperature of the solution being held below 30.degree. C. during dispersion of the carbon. The temperature of the hexamethylenetetramine-carbon mixture is reduced to 5.degree. C. and it is then mixed with 175 ml of an aqueous solution containing acid-deficient uranyl nitrate (2.43 molar) and urea (3.04 molar), the temperature of the uranyl nitrate-urea solution being at -5.degree. C. prior to mixing. The resulting mixture is discharged from a vibrating nozzle into trichloroethylene at a temperature of 65.degree. C. to form microspheres having a diameter in the range of 300-400 microns, in accordance with known procedures used in the sol-gel process of forming nuclear fuel microspheres. Preferably the microspheres thus formed are aged in the trichloroethylene for 20 minutes, and after being separated from the liquid they are dried by use of an air stream, washed with 0.5 molar ammonium hydroxide, again purged with air, and finally heated in an oven at 250.degree. C. to complete drying. The dried microspheres are calcined at 450.degree. C. to convert UO.sub.3 therein to UO.sub.2 and thereby provide precursor microspheres having a composition of UO.sub.2 and free carbon within the range given above. In accordance with this invention, microspheres having a UO.sub.2 -C composition within the stated range are sintered at 1550.degree. C. in a continuously flowing atmosphere consisting of argon and carbon monoxide, the molar percentage of CO in the atmosphere being varied in a manner described hereinafter. Since the CO-Ar atmosphere is continuously removed from the furnace in which the UO.sub.2 -C microspheres are sintered, the carbothermic reduction reaction proceeds toward UC.sub.2. In the portion of the U-C-O phase diagram shown in FIG. 2, the letter a designates a microsphere composition of UO.sub.2 and free carbon which is suitable as an initial composition for forming microspheres in accordance with the invention (namely, a composition in the middle of the range of UO.sub.2 -C usable in the process of the invention). As the carbothermic reduction of the initial UO.sub.2 /C composition proceeds, the composition of the microspheres will change to include different amounts of UO.sub.2, UC.sub.2, and free C, these compositions lying on the broken line between points a and b. The amount of free C in the microspheres will gradually decrease until point b is reached, when the microspheres will contain only UC.sub.2 and UO.sub.2. The composition of the microspheres can also be varied along the broken line between points b, c and d, and beyond point d, as determined by partial pressure of CO in the CO/inert gas atmosphere present in the furnace in which the microspheres are sintered. This dependence of the composition of the microspheres on the CO partial pressure in the furnace atmosphere is depicted in FIG. 3, wherein the initial composition of UO.sub.2 +free C is represented as point a. The composition moves into the three-phase region UO.sub.2 +UC.sub.2 +C (toward point b in FIG. 2) only if the partial pressure of CO(P.sub.CO) in the furnace atmosphere is less than level 1 in FIG. 3. According to the Gibbs phase rule, there is one degree of freedom within the three-phase region. Therefore for a given temperature, the equilibrium pressure of CO is constant and independent of the quantities of the three solid phases. When the tie line joining UC.sub.2 and UO.sub.2 is reached at point b, the equilibrium CO pressure will drop to a lower level (at point b' in FIG. 3). The equilibrium CO pressure over the three-phase region UC.sub.x O.sub.y +UO.sub.2 +UC.sub.2 is also constant (level 2 in FIG. 3 between points b' and c). The reaction will proceed into this three-phase region only if the P.sub.CO in the furnace atmosphere is less than level 2 in FIG. 3. The reaction will continue into the two-phase region UO.sub.2 +UC.sub.x O.sub.y if the P.sub.CO in the furnace is less than level 2. The Gibbs phase rule shows that there are two degrees of freedom in a two-phase region. Therefore at any temperature P.sub.CO over the UO.sub.2 and UC.sub.x O.sub.y will vary as the quantity of the two solid phases varies (line c--d in FIG. 3). Therefore the final composition of microspheres sintered in an atmosphere containing CO can be controlled by regulating the partial pressure of CO in the gas stream entering the sintering furnace. If the P.sub.CO is above level 1, no reaction will occur. If the P.sub.CO is between level 1 and level 2, UO.sub.2 and UC.sub.2 will be produced. If the P.sub.CO is between level 2 and level 3, the reaction will proceed into the UO.sub.2 +UC.sub.x O.sub.y phase region. FIG. 4 illustrates the above-described process conditions with greater particularity. Thermodynamic data for the U-C-O system show that atmospheres containing from about 1.2 to 1.9% CO will produce the phases UO.sub.2 and UC.sub.2 at 1550.degree. C. A sintering atmosphere containing less than 1.2% CO will produce UO.sub.2 and UC.sub.x O.sub.y while an atmosphere containing more than 1.9% CO will produce no reaction and leave UO.sub.2 and carbon in microspheres placed in such an atmosphere. Thus at a temperature of 1550.degree. C. the value 1.9% CO corresponds to level 1 of FIG. 3 and the value 1.2% CO corresponds to level 2 of FIG. 3. In accordance with this invention microspheres having the composition of UO.sub.2 and free carbon represented by point a in FIG. 2 are initially sintered in a furnace under a flowing gas consisting of about 0.5 to 1 mole percent CO and 99% to 99.5% Ar, which causes the microsphere composition to change to UO.sub.2 plus UC.sub.x O.sub.y. This process step produces microspheres of very high density (approaching 11 g/cm.sup.3). It would not be desirable to change the composition of the microspheres to UO.sub.2 +UC.sub.2 directly by use of an atmosphere comprising between 1.2 to 1.9% CO because microspheres so produced would have an unacceptable low density (5-8g/cm.sup.3). It would appear from examination of FIG. 4 that a second sintering period at 1550.degree. C. under an atmosphere containing more than 1.9% CO would change the composition of the microspheres back to UO.sub.2 +free carbon. However, it has been found that sintering the microspheres which have been converted to UO.sub.2 +UC.sub.x O.sub.y at a temperature of 1550.degree. C. under an atmosphere consisting of 3 mole percent CO and 97 mole percent Ar instead produces microspheres containing UC.sub.2 and UO.sub.2 within the desired composition range of 1-30 mole percent UC.sub.2 and 70-99 mole percent UO.sub.2. Furthermore these microspheres have the required high density in the range of about 10.2 to 11.0 g/cm.sup. 3. A sintering furnace used in forming reactor fuel microspheres in accordance with this invention can consist of a tube furnace having a diameter of 3.8 cm. Molybdenum carbide crucibles can be used to hold the microspheres to prevent any reaction between UO.sub.2 -UC.sub.2 and the crucible. The microspheres in the furnace are exposed to a flowing atmosphere containing accurately controlled amounts of CO and Ar. Microspheres containing between 45 to 97 mole percent UO.sub.2 and between 3 to 55 mole percent free carbon are first sintered at 1550.degree. C. in a flowing atmosphere consisting of 1 mole percent CO and 99 mole percent Ar for 4 hours. The microspheres are then sintered at 1550.degree. C. in a flowing atmosphere consisting of 3 mole percent CO and 97 mole percent Ar for an additional 4 hours. By way of example, the following microsphere compositions were obtained by the above-described process steps. ______________________________________ INI- INI- TIAL TIAL FINAL FINAL FINAL MOLE MOLE MOLE MOLE DENSITY SAMPLE % UO.sub.2 % C % UO.sub.2 % UC.sub.2 g/cm.sup.3 ______________________________________ 1 69.9 30.1 88.9 11.1 10.29 2 60.4 39.6 83.5 16.5 10.22 3 54.9 45.1 79.7 20.3 10.72 4 53.2 46.8 77.5 22.5 10.64 ______________________________________ The composition of the UO.sub.2 -UC.sub.2 microspheres obtained by the described process steps was established by chemical analysis and x-ray diffraction procedures.