GB829094A - Production of uranium peroxide - Google Patents
Production of uranium peroxideInfo
- Publication number
- GB829094A GB829094A GB7052/46A GB705246A GB829094A GB 829094 A GB829094 A GB 829094A GB 7052/46 A GB7052/46 A GB 7052/46A GB 705246 A GB705246 A GB 705246A GB 829094 A GB829094 A GB 829094A
- Authority
- GB
- United Kingdom
- Prior art keywords
- uranium
- solution
- added
- sulphate
- peroxide
- 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)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Uranium peroxide is precipitated from an aqueous uranyl salt solution, particularly the sulphate, containing magnesium and fluorine, by effecting the precipitation in the presence of a substantial amount of ammonium sulphate, which holds fluorine in solution and improves the crystalline form of the uranium peroxide obtained. Aqueous uranyl sulphate starting solutions preferably contain between 3 and 16% of uranyl sulphate and between 1 and 2 1/2 mols. of ammonium sulphate are added for each mol. of uranyl sulphate. The pH is preferably between 2 and 4 and sufficient hydrogen peroxide or alkali metal peroxide is then added to precipitate the uranium peroxide, the pH of the solution being adjusted by acid or alkali during the precipitation. The precipitation should be effected below 65 DEG C. and preferably at at least 30 DEG C., and the crystalline uranium peroxide formed should be separated from the solution promptly to avoid fluorine contamination. According to examples: (1) slag obtained in the production of uranium metal by reduction of uranium tetrafluoride by magnesium was air roasted and treated with dilute sulphuric acid. Hydrogen peroxide was added to convert tetravalent uranium to hexavalent and calcium carbonate was added to bring the pH to 3.7. The mixture was maintained at 85 DEG to 90 DEG C. and then filtered; the filter cake washing and filtrate were combined to provide an uranyl sulphate starting solution. Ammonium sulphate was added and the pH adjusted to 2.9 with caustic soda solution. Precipitation of uranium peroxide was effected with aqueous hydrogen peroxide. (3) a uranyl sulphate solution obtained by calcining uranium dross containing magnesium and fluorine, with quick lime, digesting the calcined product in aqueous sulphuric acid at 90 DEG to 95 DEG C., neutralizing with calcium carbonate to a pH of 3.5 and filtering, was used as the starting solution. Ammonium sulphate was added and the solution was acidified to pH 3 with dilute sulphuric acid and cooled to 40 DEG C. After filtering 27.5% hydrogen peroxide solution was added beneath the surface during which addition the pH fell to 1.5; aqueous ammonium hydroxide was added to restore the pH to 3. Precipitated uranium peroxide was separated from the mother liquor by centrifuging and after washing with distilled water at 60 DEG C. contained less than 0.2% of fluorine. Specifications 829,088 and 829,091 are referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US829094XA | 1945-03-15 | 1945-03-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB829094A true GB829094A (en) | 1960-02-24 |
Family
ID=22174237
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB7052/46A Expired GB829094A (en) | 1945-03-15 | 1946-03-06 | Production of uranium peroxide |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB829094A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112707444A (en) * | 2020-12-10 | 2021-04-27 | 核工业北京化工冶金研究院 | Method for preparing uranium oxide from uranium-containing ammonium sulfate solution |
-
1946
- 1946-03-06 GB GB7052/46A patent/GB829094A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112707444A (en) * | 2020-12-10 | 2021-04-27 | 核工业北京化工冶金研究院 | Method for preparing uranium oxide from uranium-containing ammonium sulfate solution |
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