Patent Number: 041586816
Section: claims

1. Method for sintering nuclear fuel pellets selected from the group consisting of nuclear fuel oxides and mixtures of nuclear fuel oxides having oxygen in stoichiometric excess of the dioxide in a reducing furnace atmoshpere, which comprises (a) passing the nuclear fuel pellets having a stoichiometric excess of oxygen through a heated reduction furnace with a reducing atmosphere to effect reduction of at least substantially all said oxygen in stoichiometric excess of the dioxide,  (b) regulating the residence time of said nuclear fuel oxides in said reducing furnace to produce said reduced nuclear fuel oxides,  (c) cooling said reduced nuclear fuel oxides,  (d) passing said cooled-down nuclear fuel oxides to an intermediate station,  (e) subsequently passing said cooled-down nuclear fuel oxides through a separate sintering furnace, and  (f) independently regulating the residence time of the nuclear fuel oxides passing through the sintering furnace to effect sintering of the nuclear fuel pellets.  (a) passing the nuclear fuel pellets having a stoichiometric excess of oxygen through a heated reduction furnace with a reducing atmosphere to effect reduction of at least substantially all said oxygen in stoichiometric excess of the dioxide,  (b) regulating the residence time of said nuclear fuel oxides in said reducing furnace to produce said reduced nuclear fuel oxides,  (c) cooling said reduced nuclear fuel oxides,  (d) passing said cooled-down nuclear fuel oxides to an intermediate station,  (e) subsequently passing said cooled-down nuclear fuel oxides through a separate sintering furnace,  (f) independently regulating the residence time of the nuclear fuel oxides passing through the sintering furnace to effect sintering of the nuclear fuel pellets, and  (g) wherein the nuclear fuel pellets are treated in the two separated furnaces at different temperatures and the gas atmospheres in the two furnaces are independent of each other and have different compositions.  (a) passing the nuclear fuel pellets having a stoichiometric excess of oxygen through a heated reduction furnace with a reducing atmosphere to effect reduction of at least substantially all said oxygen in stoichiometric excess of the dioxide,  (b) regulating the residence time of said nuclear fuel oxides in said reducing furnace to produce said reduced nuclear fuel oxides,  (c) cooling said reduced nuclear fuel oxides,  (d) passing said cooled-down nuclear fuel oxides to an intermediate station,  (e) subsequently passing said cooled-down nuclear fuel oxides through a separate sintering furnace,  (f) independently regulating the residence time of the nuclear fuel oxides passing through the sintering furnace to effect sintering of the nuclear fuel pellets, and  (g) wherein the nuclear fuel pellets are treated in the two separated furnaces at different temperatures and the gas atmospheres in the two furnaces are independent of each other and the amounts of gas fed to each furnace are different. 2. Method for sintering nuclear fuel pellets selected from the group consisting of nuclear fuel oxides and mixtures of nuclear fuel oxides having oxygen in stoichiometric excess of the dioxide in a reducing furnace atmosphere, which comprises 3. Method for sintering nuclear fuel pellets selected from the group consisting of nuclear fuel oxides and mixtures of nuclear fuel oxides having oxygen in stoichiometric excess of the dioxide in a reducing furnace atmosphere, which comprises 4. Method according to claim 2, wherein the gas atmosphere in the reduction furnace has a humidity concentration different from the humidity concentration in the gas atmosphere in the sintering furnace. 5. Method according to claim 3, wherein the gas atmosphere in the reduction furnace has a humidity concentration different from the humidity concentration in the gas atmosphere in the sintering furnace. 6. Method according to claim 2, wherein the nuclear fuel pellets are cooled down to a temperature below 100.degree. C. between the two furnaces. 7. Method according to claim 2, wherein a gas mixture of N.sub.2 and 4 to 8% H.sub.2 is introduced into the reduction furnace to supply the gas atmosphere therein, and wherein a gas mixture of rare gas and 4 to 8% H.sub.2 is introduced into the sintering furnace to supply the gas atmosphere therein. 8. Method according to claim 2, wherein a gas mixture of N.sub.2 and 4 to 12% CO is introduced into the reduction furnace to supply the gas atmosphere therein, and wherein a gas mixture of rare gas and 4 to 8% H.sub.2 is introduced into the sintering furnace to supply the gas atmosphere therein. 9. Method according to claim 7, wherein the rare gas is argon. 10. Method according to claim 8, wherein the rare gas is argon. 11. Method according to claim 2, wherein the nuclear fuel pellets in the reduction furnace are heated to a temperature in the range of 700.degree. C. to about 1000.degree. C., and wherein the pellets in the sintering furnace are heated to a temperature in the range of about 1000.degree. C. and 1760.degree. C. 12. Method according to claim 3, wherein reducing gas introduced in the reduction furnace to provide a reducing atmosphere flows counter-current to the passage of nuclear fuel pellets therein, and the flow of gas relative to the passage of pellets regulated to limit the gas content of H.sub.2 0 at the furnace exit to 0.8% by volume H.sub.2 O. 13. Method according to claim 2, wherein the gas in the sintering furnace is additionally humidified up to a ratio of H.sub.2 : H.sub.2 O in the gas of 10:1. 14. Method according to claim 2, wherein reducing gas is introduced in the reduction furnace to provide a reducing atmosphere and is discharged from the reduction furnace, and wherein the discharged gas is cooled to condense condensible constituents entrained by the gas in the reduction furnace, and the condensed constituents separated from the gas. 15. Method according to claim 14, wherein the gas discharged from the reduction furnace is passed through an electrostatic dust separator to remove dust particles contained in the gas. 16. Method according to claim 2, wherein reducing gas is introduced in the reduction furnace at a plurality of spaced points along the length of the furnace. 17. Method according to claim 2, wherein the pellets in the sintering furnace are internally heated and the outer wall of the sintering furnace externally cooled.