Patent US3987145A successfully refreshed from Google Patents.
US3987145A
Expired / Lapsed
US
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Ferric ion as a scavenging agent in a solvent extraction process
Assignee: Energy Research and Development Administration ERDA
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Filing: 1975-05-15
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Granted: 1976-10-19
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Expires: 1995-05-15
Abstract
Abstract Ferric ions are added into the aqueous feed of a plutonium scrap recovery process that employs a tributyl phosphate extractant. Radiolytic degradation products of tributyl phosphate such as dibutyl phosphate form a solid precipitate with iron and are removed from the extraction stages via the waste stream. Consequently, the solvent extraction characteristics are improved, particularly in respect to minimizing the formation of nonstrippable plutonium complexes in the stripping stages. The method is expected to be also applicable to the partitioning of plutonium and uranium in a scrap recovery process.
Inventors
- 👤 Lester E. Bruns
- 👤 Earl C. Martin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 13:05
CPC Classifications
C; C01; C01G; C01G56/00; C01G56/001; C22; C22B; C22B60/00; C22B60/02; C22B60/0204; C22B60/0217; C22B60/0252; C22B60/026; C22B60/0291; C22B60/0295; C22B60/04; G; G21; G21C; G21C19/00; G21C19/42; G21C19/44; G21C19/46; Y; Y02; Y02E; Y02E30/00; Y02E30/30; Y02P; Y02P10/00; Y02P10/20; Y02W; Y02W30/00; Y02W30/50
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
157 words
In a process for recovering actinide values from an aqueous feed solution containing said values along with cations of lower atomic weight, wherein within a first portion of said process, said actinide values are extracted from said aqueous solution into an organic solvent, said solvent having a greater density than said aqueous solution and containing tributyl phosphate and degradation products of tributyl phosphate, said solvent and aqueous solution forming a liquid-liquid interface within the first portion of said process with said solvent the lower layer and said aqueous solution the upper layer and wherein within a second portion of said process, at least one species of said actinide values are stripped into an aqueous strip solution, the improvement comprising adding ferric ions into said aqueous feed solution and withdrawing the resulting precipitate of said degradation products with ferric ions from said first portion of said process at said interface of said organic solvent and said aqueous solution.
Claim 2
Dependent Claim
157 words
In a process for recovering actinide values from an aqueous feed solution containing said values along with cations of lower atomic weight, wherein within a first portion of said process, said actinide values are extracted from said aqueous solution into an organic solvent, said solvent having a greater density than said aqueous solution and containing tributyl phosphate and degradation products of tributyl phosphate, said solvent and aqueous solution forming a liquid-liquid interface within the first portion of said process with said solvent the lower layer and said aqueous solution the upper layer and wherein within a second portion of said process, at least one species of said actinide values are stripped into an aqueous strip solution, the improvement comprising adding ferric ions into said aqueous feed solution and withdrawing the resulting precipitate of said degradation products with ferric ions from said first portion of said process at said interface of said organic solvent and said aqueous solution.
Claim 3
Dependent Claim
31 words
The process of claim 1 wherein said ferric ions are added to said aqueous feed solution as Fe(NO 3 ) 3 in sufficient amount to attain 0.01 to 0.2 molar concentration.
Claim 4
Dependent Claim
12 words
The process of claim 2 wherein said precipitate is ferric dibutyl phosphate.
Claim 5
Dependent Claim
20 words
The process of claim 1 wherein said species of actinide values stripped from the remainder of said values is Pu(III).
Claim 6
Dependent Claim
36 words
The process of claim 4 wherein said Pu(III) species is produced from plutonium species of higher oxidation states by the addition of a reductant into said aqueous strip solution within said second portion of said process.
Claim 7
Dependent Claim
11 words
The process of claim 5 wherein said reductant is hydroxylamine nitrate.
Claim 8
Dependent Claim
46 words
The process of claim 1 wherein said aqueous solution having a density of 1.05 to 1.3 gm/cc, said organic solution having a density of about 1.4 to 1.6 gm/cc, and said degradation product precipitate having a density intermediate the density of said aqueous and organic solutions.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-10-19 | 1980-04-19 | 1980-10-19 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-10-19 | 1984-04-19 | 1984-10-19 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-10-19 | 1988-04-19 | 1988-10-19 | $7700.00 | Window Closed / Lapsed |