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US4011296A Expired / Lapsed US ⏱️ 0.0 years remaining

Irradiated fuel reprocessing

Assignee: General Electric Co
•
Filing: 1975-05-27
•
Granted: 1977-03-08
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Expires: 1995-05-27
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Abstract

Abstract A process for separately recovering uranium, plutonium and neptunium substantially free of fission products from irradiated nuclear fuel is presented in which the fuel is dissolved in a strong mineral acid forming an aqueous dissolved nuclear fuel solution and treated to separate the uranium, plutonium and neptunium therefrom substantially free of said fission products by the sequential steps of solvent extraction, ion exchange and fluorination. The process has an improvement comprising the addition of a sufficient quantity of an additive of a stable metallic complex to the aqueous dissolved nuclear fuel solution prior to solvent extraction. This achieves improved purity of the separated uranium, plutonium and neptunium.

Inventors

  • 👤 Carl Phillip Ruiz
  • 👤 John Paul Peterson, Jr.

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 15:32
CPC Classifications
C; C01; C01G; C01G43/00; C01G43/04; C01G43/06; C01G43/063; C01G43/066; C01G56/00; C01G56/001; G; G21; G21C; G21C19/00; G21C19/42; G21C19/44; G21C19/46; G21F; G21F9/00; G21F9/007; Y; Y02; Y02E; Y02E30/00; Y02E30/30; Y02W; Y02W30/00; Y02W30/50

Claims Analysis

Total Claims: 26
Claim 1
Independent Claim 151 words
In a process for treating irradiated nuclear fuel to recover uranium and at least one transuranic isotope selected from the group consisting of neptunium and plutonium so that said uranium and said at least one transuranic isotope are substantially free of fission products which comprises dissolving said fuel in a strong mineral acid and forming an aqueous dissolved nuclear fuel solution and subsequentially treating said dissolved solution to separate said uranium and said at least one transuranic isotope therefrom substantially free of said fission products, the improvement comprising adding to said solution prior to treatment for separation of said uranium and said transuranic isotope a sufficient amount of an additive of a non-radioactive [stable ] metallic complex in which the metallic component is selected from the group consisting of niobium, tantalum and combinations thereof and said amount is sufficient to alter the decontamination factor exhibited by radioactive niobium in said solution.
Claim 2
Dependent Claim 151 words
In a process for treating irradiated nuclear fuel to recover uranium and at least one transuranic isotope selected from the group consisting of neptunium and plutonium so that said uranium and said at least one transuranic isotope are substantially free of fission products which comprises dissolving said fuel in a strong mineral acid and forming an aqueous dissolved nuclear fuel solution and subsequentially treating said dissolved solution to separate said uranium and said at least one transuranic isotope therefrom substantially free of said fission products, the improvement comprising adding to said solution prior to treatment for separation of said uranium and said transuranic isotope a sufficient amount of an additive of a non-radioactive [stable ] metallic complex in which the metallic component is selected from the group consisting of niobium, tantalum and combinations thereof and said amount is sufficient to alter the decontamination factor exhibited by radioactive niobium in said solution.
Claim 3
Dependent Claim 17 words
The process of claim 1 in which the additive is a niobium complex in a mineral acid.
Claim 4
Dependent Claim 12 words
The process of claim 2 in which the acid is nitric acid.
Claim 5
Dependent Claim 14 words
The process of claim 2 in which the additive is a niobium proxide complex.
Claim 6
Dependent Claim 14 words
The process of claim 2 in which the additive is a niobium oxalate complex.
Claim 7
Dependent Claim 14 words
The process of claim 2 in which the additive is a niobium tartrate complex.
Claim 8
Dependent Claim 14 words
The process of claim 1 in which the additive is a tantalum proxide complex.
Claim 9
Dependent Claim 14 words
The process of claim 1 in which the additive is a tantalum oxalate complex.
Claim 10
Dependent Claim 14 words
The process of claim 1 in which the additive is a tantalum tartrate complex.
Claim 11
Dependent Claim 30 words
The process of claim 1 in which the additive is present in an amount of about 10 - 6 to about 10 - 3 moles per liter of said solution.
Claim 12
Dependent Claim 19 words
The process of claim 1 in which an oxidant is added to said solution with said stable metallic complex.
Claim 13
Dependent Claim 21 words
The process of claim 1 in which the oxidant is selected from the group consisting of potassium bromate and potassium permanganate.
Claim 14
Dependent Claim 300 words
A process for treating irradiated nuclear fuel contained in clad rods to recover separately uranium, neptunium, and plutonium therefrom substantially free of fission products, said process comprising the steps of a. perforating the clad of the rods, b. contacting the perforated rods with a strong mineral acid to dissolve the nuclear fuel and form an acid dissolver solution, c. adding to said dissolver solution an additive of a nonradioactive metallic complex in an amount sufficient to alter the decontamination factor of radioactive niobium in said dissolver solution, said complex having the metallic component selected from the group consisting of niobium, tantalum and combinations thereof, d. contacting said dissolver solution with an organic solvent to separate uranium, plutonium and neptunium into the organic solvent from said dissolver solution and leave an aqueous solvent extraction raffinate containing fission products, e. contacting the organic solvent with a dilute mineral acid to strip the uranium, plutonium and neptunium from the organic solvent and from an aqueous extraction product, f. adjusting the valence of plutonium and neptunium by contacting said aqueous solvent extraction product with a reductant, g. concentrating said aqueous extraction product, g. cooling said concentrated aqueous solvent extraction product, i. contacting said concentrated aqueous solvent extraction product with an anion exchange resin so that plutonium in the +4 valence is extracted by the resin, leaving a first aqueous anion exchange raffinate containing neptunium and uranium, j. adjusting the valence of the neptunium in said first aqueous anion exchange raffinate with a reductant, k. contacting said first aqueous anion exchange raffinate with an anion exchange resin to extract the neptunium therefrom, and giving a second aqueous anion exchange raffinate, l. dehydrating said second aqueous anion exchange raffinate to an anhydrous solid of uranium oxide, and m. fluorinating the anhydrous solid to give uranium hexafluoride.
Claim 15
Dependent Claim 300 words
A process for treating irradiated nuclear fuel contained in clad rods to recover separately uranium, neptunium, and plutonium therefrom substantially free of fission products, said process comprising the steps of a. perforating the clad of the rods, b. contacting the perforated rods with a strong mineral acid to dissolve the nuclear fuel and form an acid dissolver solution, c. adding to said dissolver solution an additive of a nonradioactive metallic complex in an amount sufficient to alter the decontamination factor of radioactive niobium in said dissolver solution, said complex having the metallic component selected from the group consisting of niobium, tantalum and combinations thereof, d. contacting said dissolver solution with an organic solvent to separate uranium, plutonium and neptunium into the organic solvent from said dissolver solution and leave an aqueous solvent extraction raffinate containing fission products, e. contacting the organic solvent with a dilute mineral acid to strip the uranium, plutonium and neptunium from the organic solvent and from an aqueous extraction product, f. adjusting the valence of plutonium and neptunium by contacting said aqueous solvent extraction product with a reductant, g. concentrating said aqueous extraction product, g. cooling said concentrated aqueous solvent extraction product, i. contacting said concentrated aqueous solvent extraction product with an anion exchange resin so that plutonium in the +4 valence is extracted by the resin, leaving a first aqueous anion exchange raffinate containing neptunium and uranium, j. adjusting the valence of the neptunium in said first aqueous anion exchange raffinate with a reductant, k. contacting said first aqueous anion exchange raffinate with an anion exchange resin to extract the neptunium therefrom, and giving a second aqueous anion exchange raffinate, l. dehydrating said second aqueous anion exchange raffinate to an anhydrous solid of uranium oxide, and m. fluorinating the anhydrous solid to give uranium hexafluoride.
Claim 16
Dependent Claim 17 words
The process of claim 13 in which the additive is a niobium complex in a mineral acid.
Claim 17
Dependent Claim 12 words
The process of claim 14 in which the acid is nitric acid.
Claim 18
Dependent Claim 14 words
The process of claim 14 in which the additive is a niobium peroxide complex.
Claim 19
Dependent Claim 14 words
The process of claim 14 in which the additive is a niobium oxalate complex.
Claim 20
Dependent Claim 14 words
The process of claim 14 in which the additive is a niobium tartarate complex.
Claim 21
Dependent Claim 14 words
The process of claim 1 in which the additive is a tantalum peroxide complex.
Claim 22
Dependent Claim 14 words
The process of claim 13 in which the additive is a tantalum oxalate complex.
Claim 23
Dependent Claim 14 words
The process of claim 13 in which the additive is a tantalum tartrate complex.
Claim 24
Dependent Claim 28 words
The process of claim 13 in which the additive is present in an amount of about 10.sup. -6 to about 10.sup. -3 moles per liter of said solution.
Claim 25
Dependent Claim 19 words
The process of claim 13 in which an oxidant is added to said solution with said stable metallic complex.
Claim 26
Dependent Claim 21 words
The process of claim 13 in which the oxidant is selected from the group consisting of potassium bromate and potassium permanganate.

References Cited (Backward Citations)

US3825649A Cited
US3374068A Cited
US3432276A Cited
US3208819A Cited
US3574531A Cited
US3867510A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-03-07 1980-09-06 1981-03-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-03-07 1984-09-06 1985-03-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-03-07 1988-09-06 1989-03-08 $7700.00 Window Closed / Lapsed

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