GB829093A - Recovery of uranium by precipitation as peroxide - Google Patents
Recovery of uranium by precipitation as peroxideInfo
- Publication number
- GB829093A GB829093A GB2592/46A GB259246A GB829093A GB 829093 A GB829093 A GB 829093A GB 2592/46 A GB2592/46 A GB 2592/46A GB 259246 A GB259246 A GB 259246A GB 829093 A GB829093 A GB 829093A
- Authority
- GB
- United Kingdom
- Prior art keywords
- uranium
- peroxide
- precipitation
- added
- sulphate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B15/00—Peroxides; Peroxyhydrates; Peroxyacids or salts thereof; Superoxides; Ozonides
- C01B15/04—Metal peroxides or peroxyhydrates thereof; Metal superoxides; Metal ozonides; Peroxyhydrates thereof
- C01B15/047—Metal peroxides or peroxyhydrates thereof; Metal superoxides; Metal ozonides; Peroxyhydrates thereof of heavy metals
- C01B15/0475—Metal peroxides or peroxyhydrates thereof; Metal superoxides; Metal ozonides; Peroxyhydrates thereof of heavy metals of actinides
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Uranium peroxide is precipitated from an aqueous uranyl salt solution, particularly the sulphate, containing magnesium and fluorine, in the presence of a substantial quantity of dissolved boric acid. Solutions containing 3-16% of uranyl sulphate are preferred and 4/10 to 1 mol. of boric acid per mol. of uranyl sulphate are preferably employed, the precipitation taking place at a pH between 2 and 4 by the addition of hydrogen peroxide or an alkali metal peroxide. Adjustment of the hydrogen ion concentration during precipitation may be effected by acid or alkali and the precipitation is preferably effected at 30-65 DEG C. According to examples: (1) uranium dross obtained in the manufacture of metallic uranium by the reduction of uranium tetrafluoride with metallic magnesium, with air roasted at 850 DEG C. and the oxide formed was treated with sulphuric acid to bring the pH to 0.9. A small amount of sodium peroxide was added and the mixture heated to 90-95 DEG C. after which calcium carbonate was added and the pH adjusted to 3.7 by the addition of concentrated sulphuric acid. The mixture was filtered hot, the filter cake was flooded with water and the filtrate from the slurry and the initial filtrate were combined to obtain a starting uranyl sulphate solution. A small amount of boric acid was added and precipitation was effected with a 28% aqueous solution of hydrogen peroxide, caustic soda being added to adjust and maintain the pH at 3. The product uranium peroxide contained 0.5% of fluorine. Specification 829,088 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US829093XA | 1945-01-06 | 1945-01-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB829093A true GB829093A (en) | 1960-02-24 |
Family
ID=22174236
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2592/46A Expired GB829093A (en) | 1945-01-06 | 1946-01-25 | Recovery of uranium by precipitation as peroxide |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB829093A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20150092900A1 (en) * | 2012-04-05 | 2015-04-02 | Shine Medical Technologies, Inc. | Aqueous assembly and control method |
US10734126B2 (en) | 2011-04-28 | 2020-08-04 | SHINE Medical Technologies, LLC | Methods of separating medical isotopes from uranium solutions |
US10978214B2 (en) | 2010-01-28 | 2021-04-13 | SHINE Medical Technologies, LLC | Segmented reaction chamber for radioisotope production |
US11830637B2 (en) | 2008-05-02 | 2023-11-28 | Shine Technologies, Llc | Device and method for producing medical isotopes |
-
1946
- 1946-01-25 GB GB2592/46A patent/GB829093A/en not_active Expired
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11830637B2 (en) | 2008-05-02 | 2023-11-28 | Shine Technologies, Llc | Device and method for producing medical isotopes |
US10978214B2 (en) | 2010-01-28 | 2021-04-13 | SHINE Medical Technologies, LLC | Segmented reaction chamber for radioisotope production |
US11894157B2 (en) | 2010-01-28 | 2024-02-06 | Shine Technologies, Llc | Segmented reaction chamber for radioisotope production |
US10734126B2 (en) | 2011-04-28 | 2020-08-04 | SHINE Medical Technologies, LLC | Methods of separating medical isotopes from uranium solutions |
US20150092900A1 (en) * | 2012-04-05 | 2015-04-02 | Shine Medical Technologies, Inc. | Aqueous assembly and control method |
US11361873B2 (en) * | 2012-04-05 | 2022-06-14 | Shine Technologies, Llc | Aqueous assembly and control method |
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