GB785602A - Improvements in or relating to extraction of uranium from its ores - Google Patents
Improvements in or relating to extraction of uranium from its oresInfo
- Publication number
- GB785602A GB785602A GB2298548A GB2298548A GB785602A GB 785602 A GB785602 A GB 785602A GB 2298548 A GB2298548 A GB 2298548A GB 2298548 A GB2298548 A GB 2298548A GB 785602 A GB785602 A GB 785602A
- Authority
- GB
- United Kingdom
- Prior art keywords
- uranium
- treated
- phase
- solution
- acid
- 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
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B60/00—Obtaining metals of atomic number 87 or higher, i.e. radioactive metals
- C22B60/02—Obtaining thorium, uranium, or other actinides
- C22B60/0204—Obtaining thorium, uranium, or other actinides obtaining uranium
- C22B60/0217—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes
- C22B60/0252—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes treatment or purification of solutions or of liquors or of slurries
- C22B60/026—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes treatment or purification of solutions or of liquors or of slurries liquid-liquid extraction with or without dissolution in organic solvents
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B60/00—Obtaining metals of atomic number 87 or higher, i.e. radioactive metals
- C22B60/02—Obtaining thorium, uranium, or other actinides
- C22B60/0204—Obtaining thorium, uranium, or other actinides obtaining uranium
- C22B60/0217—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes
- C22B60/0221—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes by leaching
- C22B60/0226—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes by leaching using acidic solutions or liquors
- C22B60/0234—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes by leaching using acidic solutions or liquors sulfurated ion as active agent
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B60/00—Obtaining metals of atomic number 87 or higher, i.e. radioactive metals
- C22B60/02—Obtaining thorium, uranium, or other actinides
- C22B60/0204—Obtaining thorium, uranium, or other actinides obtaining uranium
- C22B60/0217—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes
- C22B60/0252—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes treatment or purification of solutions or of liquors or of slurries
- C22B60/0278—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes treatment or purification of solutions or of liquors or of slurries by chemical methods
- C22B60/0282—Solutions containing P ions, e.g. treatment of solutions resulting from the leaching of phosphate ores or recovery of uranium from wet-process phosphoric acid
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- General Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Geology (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Uranium is extracted from phosphatic ores containing it by treating the ore with sulphuric acid of substantially 1.84 specific gravity, to decompose phosphates present and form a system comprising a liquid sulphuric acidphosphoric acid phase and a solid phase containing substantially all of the uranium from the ore, and thereafter separating the solid phase from the liquid phase and working it up to recover uranium. The solids are preferably separated from the liquid by centrifugal means and afterwards taken up with water to dissolve the uranium and the solution treated with a soluble barium salt and filtered. The remaining solution is then treated with sodium hydroxide, ammonia or magnesium oxide to precipitate metals, including uranium, as hydroxides. Thereafter the separated and washed hydroxides are brought into nitric acid solution, from which the uranium may be extracted by means of diethyl ether or other organic solvent. According to an example, monazite was treated with sulphuric acid and heated to 220 DEG C. for two hours, and after cooling the solids were separated from the liquid. The solids were taken up with water and the resulting solution after dilution, was treated with gelatin and barium nitrate, the barium sulphate so formed acting as a collector for the mesothorium and the gelatin floculating the silica present. The filtrate was treated with caustic soda and the precipitate obtained after washing was taken up in nitric acid leaving an insoluble residue of thorium and ceric phosphates. The insoluble residue was, after separation, boiled with caustic soda, filtered, washed, dissolved in nitric acid and returned to the main solution. The combined solutions, optionally in the presence of a salting out agent such as ammonium nitrate, were subjected to a solvent extraction with, for example, a mixture of diethyl ether, tetrahydrosylvane and nitric acid, the acid being present to reduce extraction thereof from the aqueous phase. The residual aqueous solution may be treated for the recovery of thorium and rare earths whilst the organic phase contained uranium, thorium and cerium. The uranium may be recovered for example by treating the organic solvent phase with water to obtain an aqueous solution from which the uranium may be precipitated with hydrogen peroxide as uranium peroxide. Specification 781,721 is referred to.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2298548A GB785602A (en) | 1948-08-31 | 1948-08-31 | Improvements in or relating to extraction of uranium from its ores |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2298548A GB785602A (en) | 1948-08-31 | 1948-08-31 | Improvements in or relating to extraction of uranium from its ores |
Publications (1)
Publication Number | Publication Date |
---|---|
GB785602A true GB785602A (en) | 1957-10-30 |
Family
ID=10188228
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2298548A Expired GB785602A (en) | 1948-08-31 | 1948-08-31 | Improvements in or relating to extraction of uranium from its ores |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB785602A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2474056A1 (en) * | 1980-01-23 | 1981-07-24 | Israel Atomic Energy Comm | Winning uranium from phosphorite - by leaching with sulphuric acid and reducing agent so gypsum and tetra:valent uranium are coprecipitated |
EP0079190A2 (en) * | 1981-11-09 | 1983-05-18 | Exxon Research And Engineering Company | The removal of solids from wet process phosphoric acid |
CN114686681A (en) * | 2020-12-30 | 2022-07-01 | 中核通辽铀业有限责任公司 | Remote uranium deposit resource recovery system and method |
-
1948
- 1948-08-31 GB GB2298548A patent/GB785602A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2474056A1 (en) * | 1980-01-23 | 1981-07-24 | Israel Atomic Energy Comm | Winning uranium from phosphorite - by leaching with sulphuric acid and reducing agent so gypsum and tetra:valent uranium are coprecipitated |
EP0079190A2 (en) * | 1981-11-09 | 1983-05-18 | Exxon Research And Engineering Company | The removal of solids from wet process phosphoric acid |
EP0079190A3 (en) * | 1981-11-09 | 1984-02-08 | Exxon Research And Engineering Company | The removal of solids from wet process phosphoric acid |
CN114686681A (en) * | 2020-12-30 | 2022-07-01 | 中核通辽铀业有限责任公司 | Remote uranium deposit resource recovery system and method |
CN114686681B (en) * | 2020-12-30 | 2023-10-20 | 中核通辽铀业有限责任公司 | Remote uranium deposit resource recovery system and method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3104950A (en) | Process for the separation of iron and titanium values by extraction and the subsequent preparation of anhydrous titanium dopxode | |
US3052513A (en) | Stripping of uranium from organic extractants | |
GB907465A (en) | Improvements in or relating to the recovery of molybdenum and/or vanadium values | |
US2024026A (en) | Recovering lithium compounds | |
US2176610A (en) | Process of working ores of vanadium and uranium | |
US2811411A (en) | Method of processing monazite sand | |
US2021987A (en) | Recovery of values from lithium bearing ores | |
US2425573A (en) | Separation of thorium and the rareearth group from minerals | |
US3111375A (en) | Process for the separation of thorium, cerium and rare earths starting from their oxides or hydroxides | |
US2630369A (en) | Method for treating vanadium and uranium ores and the like | |
CN110306059B (en) | Method for recycling rare earth in cerium-doped lutetium yttrium silicate waste | |
GB785602A (en) | Improvements in or relating to extraction of uranium from its ores | |
US2869979A (en) | Slurry solvent extraction process for the recovery of metals from solid materials | |
US3146063A (en) | Process for separating scandium from mixtures containing scandium and thorium values | |
US4248838A (en) | Preparation of useful MgCl2. solution with subsequent recovery of KCl from carnallite | |
GB880046A (en) | Process for separation of thorium from uranium | |
US2176609A (en) | Process of extracting values from complex ores of vanadium and uranium | |
US3821354A (en) | Method for selectively abstracting nickel from an aqueous ammoniacal solution | |
US3848055A (en) | Extraction of strontium values from celestite | |
US3704091A (en) | Extraction of beryllium from ores | |
US1307153A (en) | Lonnie w | |
US3514266A (en) | Separation of aluminum,calcium,and magnesium from the alkali metals by solvent extraction | |
Shaw | Extraction of rare-earth elements from bastnaesite concentrate | |
US2298800A (en) | Process for the production of beryllium oxide or hydroxide | |
US2815262A (en) | Separation process for thorium salts |