PRODUCTION OF UO2 POWDER FROM URANYL NITRATE SERIES

PURPOSE:To obtain UO2 powder capable of pelletizing as it is by adding aqueous ammonia into an uranyl nitrate soln. of prescribed concn. controlling the addition velocity. CONSTITUTION:The precipitate of ammonium biuranate is produced by adding aqueous ammonia of 20-35% concn. to an uranyl nitrate s...

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Hauptverfasser: HAMAGUCHI KAZUHIKO, HASEGAWA SHINICHI
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HASEGAWA SHINICHI
description PURPOSE:To obtain UO2 powder capable of pelletizing as it is by adding aqueous ammonia into an uranyl nitrate soln. of prescribed concn. controlling the addition velocity. CONSTITUTION:The precipitate of ammonium biuranate is produced by adding aqueous ammonia of 20-35% concn. to an uranyl nitrate soln. of 50-100g/l uranium concn. and 0-2.5N concn. of free nitric acid while controlling the addition velocity at 0.01-0.025gNH3/min per 1g uranium in the case of 3.5-4.5 pH of the uranyl nitrate soln. and at 0.1-0.5g/min per 1b uranium in the case of >=4.5 pH thereof and holding the mixture. Then after separating and drying this precipitate, it is calcined at 660-760 deg.C for 2-4hr in an air current of 0.3-0.3M /h.kgU flow rate and then reduced for 20-1hr in the reducing atmosphere of 2-5M /h.kgU flow rate of H2 to obtain UO2 powder.
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CONSTITUTION:The precipitate of ammonium biuranate is produced by adding aqueous ammonia of 20-35% concn. to an uranyl nitrate soln. of 50-100g/l uranium concn. and 0-2.5N concn. of free nitric acid while controlling the addition velocity at 0.01-0.025gNH3/min per 1g uranium in the case of 3.5-4.5 pH of the uranyl nitrate soln. and at 0.1-0.5g/min per 1b uranium in the case of &gt;=4.5 pH thereof and holding the mixture. 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CONSTITUTION:The precipitate of ammonium biuranate is produced by adding aqueous ammonia of 20-35% concn. to an uranyl nitrate soln. of 50-100g/l uranium concn. and 0-2.5N concn. of free nitric acid while controlling the addition velocity at 0.01-0.025gNH3/min per 1g uranium in the case of 3.5-4.5 pH of the uranyl nitrate soln. and at 0.1-0.5g/min per 1b uranium in the case of &gt;=4.5 pH thereof and holding the mixture. Then after separating and drying this precipitate, it is calcined at 660-760 deg.C for 2-4hr in an air current of 0.3-0.3M /h.kgU flow rate and then reduced for 20-1hr in the reducing atmosphere of 2-5M /h.kgU flow rate of H2 to obtain UO2 powder.</abstract><oa>free_for_read</oa></addata></record>
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subjects CHEMISTRY
COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSESC01D OR C01F
INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OFSOLID INORGANIC COMPOUNDS
INORGANIC CHEMISTRY
METALLURGY
NUCLEAR ENGINEERING
NUCLEAR PHYSICS
NUCLEAR REACTORS
PHYSICS
title PRODUCTION OF UO2 POWDER FROM URANYL NITRATE SERIES
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