2013
DOI: 10.1007/s10967-013-2756-8
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UO2, NpO2 and PuO2 preparation in aqueous nitrate solutions in the presence of hydrazine hydrate

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Cited by 8 publications
(6 citation statements)
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“…As we showed previously [1][2][3], hydrated uranium dioxide UO 2 ·nH 2 O prepared in UO 2 (NO 3 ) 2 solutions in the presence of hydrazine hydrate (HH) at ~90°С in 48 h in the course of subsequent heat treatment in an electrical resistance furnace transforms into various oxides depending on the conditions: into UO 2 in an inert or reducing atmosphere in the interval 280-800°С, into UO 3 in air at 440°С, and into U 3 O 8 in the interval 570-800°С. The drawbacks of this process are the presence of residual mother liquors and relatively low rate of the transformation of UO 2 (NO 3 ) 2 into UO 2 ·nH 2 O.…”
supporting
confidence: 68%
“…As we showed previously [1][2][3], hydrated uranium dioxide UO 2 ·nH 2 O prepared in UO 2 (NO 3 ) 2 solutions in the presence of hydrazine hydrate (HH) at ~90°С in 48 h in the course of subsequent heat treatment in an electrical resistance furnace transforms into various oxides depending on the conditions: into UO 2 in an inert or reducing atmosphere in the interval 280-800°С, into UO 3 in air at 440°С, and into U 3 O 8 in the interval 570-800°С. The drawbacks of this process are the presence of residual mother liquors and relatively low rate of the transformation of UO 2 (NO 3 ) 2 into UO 2 ·nH 2 O.…”
supporting
confidence: 68%
“…For smaller scale, µg reactions, calcination of ion-exchange resins is also possible [179]. Synthesis of polycrystalline samples of actinide oxides have also been reported through sol-gel [53] and aqueous routes [72,124,130]. Many of the actinide oxides can be hypo-or hyperstoichiometric, i.e.…”
Section: Crystal Growthmentioning
confidence: 99%
“…To avoid accumulation of fluoride in the bottoms, the process should be performed under strongly acidic conditions [25] at reduced residual pressure to decrease the temperature and thus to avoid intense corrosion of tubes of the heating chamber. The bottoms are continuously fed from the evaporator to final evaporator to distill off the residual amounts of hydrofluoric acid by steam treatment on plates, with the subsequent delivery to the HLW calcination unit.…”
Section: Concentration Of Process Hlw and Recycled Ilwmentioning
confidence: 99%