Purification of plutonium
AssigneeBritish Nuclear Fuels plc
InventorsEdward S. Chapman, William Smith
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AssigneeBritish Nuclear Fuels plc
InventorsEdward S. Chapman, William Smith
Estimating the term…
During the reprocessing of irradiated nuclear fuel by solvent extraction techniques a primary separation to give a uranium containing product stream and a plutonium containing product stream occurs. The plutonium in the plutonium containing stream is separated from neptunium and uranium by bringing a solution containing plutonium, neptunium and uranium in an organic solvent into contact first with an aqueous solution of a hydroxylamine and/or a hydrazine salt at 30.degree. to 35.degree. C. to preferentially reduce the neptunium and to extract it into the aqueous phase and then bringing the organic solution containing plutonium and uranium into contact with an aqueous phase containing a hydroxylamine and a hydrazine salt at about 50.degree. C. to preferentially reduce the plutonium and to extract it into the aqueous phase leaving the uranium in the organic solvent.
A process for the purification of a plutonium-containing aqueous phase during the reprocessing of irradiated nuclear fuel in which the aqueous phase also contains some uranium and neptunium includes the steps of bringing the plutonium-containing aqueous phase into contact with an organic solvent, which solvent comprises a solution of an alkyl ester of phosphoric acid in an organic diluent, to extract plutonium, uranium and neptunium into solution in the organic solvent, bringing the organic solution into contact with a first aqueous phase containing a reductant for neptunium selected from the group consisting of hydroxylamine salts, hydrazine salts and mixtures of hydroxylamine and hydrazine salts at about 30.degree. to 35.degree. C. to extract neptunium into the aqueous phase, separating the organic solution from the aqueous phase, bringing the organic solution into contact with a further aqueous phase containing a reductant for plutonium selected from the group consisting of hydroxylamine salts, hydrazine salts and mixtures of hydroxylamine and hydrazine salts at about 50.degree. C. to extract plutonium into the further aqueous phase and separating the organic solvent from the further aqueous phase.
Dependencies are inferred from the claim text.