GB679546A - Improved process for the extraction of rhenium and analogous elements - Google Patents
Improved process for the extraction of rhenium and analogous elementsInfo
- Publication number
- GB679546A GB679546A GB553649A GB553649A GB679546A GB 679546 A GB679546 A GB 679546A GB 553649 A GB553649 A GB 553649A GB 553649 A GB553649 A GB 553649A GB 679546 A GB679546 A GB 679546A
- Authority
- GB
- United Kingdom
- Prior art keywords
- rhenium
- solution
- organic
- acid
- extracted
- 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
- C22B61/00—Obtaining metals not elsewhere provided for in this subclass
-
- 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
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Elements of column VII of the Periodic classification, particularly manganese, technecium, rhenium and neptunium are extracted from raw materials containing them, even in traces, by attacking the material with an oxidizing chemical to form a solution containing the elements as anions, adding to the solution a water-soluble salt of an organic base <FORM:0679546/IV (b)/1> wherein R1-RIV are organic radicals, M is an element of column V of the Periodic classification (N, P, As, Sb, Bi, &) and Ss an anion, so as to form compounds containing anions of the elements and cations of the organic base, and extracting said compounds with an organic solvent, e.g. chloroform, bromoform or dichloroethane. Rhenium is thus extracted as a perrhenate, manganese as a permanganate, chlorine as a perchlorate and iodine as an iodide, iodate or periodate Rhenium and technecium should be extracted in an alkaline medium when molybdenum is present, and rhenium and manganese in an acid medium when they are to be separated from a solution containing iron. The invention is particularly described with reference to the extraction of rhenium from molybdenite ore.ALSO:Elements of column VII of the Periodic Classification, particularly manganses, technetium, rhenium and neptunium, are extracted from raw materials containing them, even in traces by attacking the materials with an oxidising chemical to form a solution containing the elements as anions, adding to the solution a water soluble salt of an organic base <FORM:0679546/III/1> wherein R1-R1v are organic radicals, M is an element of column V of the Periodic Classification (N, P, As, St, Bi &c.) and Ss an anion, sco as to form compounds containing anions of the elements and cations of the organic base, and extracting said compounds with an organic solvent, e.g. chloroform, bromoform or dichloroethane. Rhenium is thus extracted as a perrhenate, manganese as a permanganate, chlorine as a perchlorate, and iodine as an iodide, iodate or periodate. Rhenium and technetium should be extracted in an alkaline medium when molybdenum is present, and rhenium and manganese in an acid medium when they are to be separated from a solution containing iron. The invention is particularly described with reference to the extraction of rhenium from molybdenite ore, which is attacked by fuming nitric acid at 60-80 DEG C, or with sodium dioxide. In the first case, excess nitric acid is removed, and then the solution is brought to, say pH9. The organic reagent, e.g. tetraphenylarsonium or phosphonium chloride, or triphenylbenzyl phosphonium chloride, is added, and the mixture then shaken with the organic solvent. The organic solution is dried with calcium chloride, and agitated with 12N hydrochloric acid, or with a concentrated acid and a reducing agent such as stannous chloride, or with a concentrated solution of a metal chloride, whereby rhenium passes into the aqueous phase whilst the organic solvent contains the organic reagent. Alternatively, the organic base may be precipitated by adding N/10 perchloric acid. The rhenium-containing solution is evaporated until perrhenic acid begins to distil, the solution is neutralized with soda or ammonia and evaporated to dryness, and the residue reduced to rhenium by hydrogen at 1000 DEG C. Another example describes the extraction of technetium, produced by irradiating molybdenum trioxide with neutrons. The irradiated material is dissolved in caustic soda, the pH adjusted to 9-11, and the extraction is effected with triphenyl arsonium chloride. The metal is produced as indicated for rhenium. A further example refers to the solubitly of tetraphenyl arsonium chlorate and periodate in water and chloroform.ALSO:A hydrochloric acid solution containing perrhenate ions is evaporated until perrhenic acid begins to distil, the solution is neutralized with soda or ammonia and evaporated to dryness, and the residue reduced to rhenium in hydrogen at 1000 DEG C. Metallic technecium is similarly produced.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR679546X | 1948-03-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB679546A true GB679546A (en) | 1952-09-17 |
Family
ID=9021736
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB553649A Expired GB679546A (en) | 1948-03-06 | 1949-03-01 | Improved process for the extraction of rhenium and analogous elements |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB679546A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0113912A2 (en) * | 1983-01-13 | 1984-07-25 | American Cyanamid Company | Selective extraction of rhenium from aqueous sulfuric acid solutions |
WO2010102391A1 (en) * | 2009-03-13 | 2010-09-16 | Recapture Metals Limited | Rhenium recovery |
-
1949
- 1949-03-01 GB GB553649A patent/GB679546A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0113912A2 (en) * | 1983-01-13 | 1984-07-25 | American Cyanamid Company | Selective extraction of rhenium from aqueous sulfuric acid solutions |
EP0113912A3 (en) * | 1983-01-13 | 1986-03-19 | American Cyanamid Company | Selective extraction of rhenium from aqueous sulfuric acid solutions |
WO2010102391A1 (en) * | 2009-03-13 | 2010-09-16 | Recapture Metals Limited | Rhenium recovery |
US8956582B2 (en) | 2009-03-13 | 2015-02-17 | Maritime House Metals Inc. | Rhenium recovery |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP7089616B2 (en) | Methods for Selectively Leaching and Extracting Precious Metals in Organic Solvents | |
GB679546A (en) | Improved process for the extraction of rhenium and analogous elements | |
US3353950A (en) | Process for the production of finely particulate high purity copper powder | |
JP4452837B2 (en) | Extraction separation method | |
US4293528A (en) | Yellowcake processing in uranium recovery | |
US2634280A (en) | Process for the extraction of rhenium and analogous elements | |
GB1094849A (en) | Process for purifying nickel sulphide | |
Ugarte et al. | Characterisation of high-temperature arsenic-containing residues from hydrometallurgical processes | |
JPH04107230A (en) | Method for extracting gold and silver from ore | |
US1902735A (en) | Process for treating material containing tin | |
US3464783A (en) | Process for working up ores which contain tungsten | |
CN106957276A (en) | The preparation method of dichlord isocyanurice acid | |
Alian et al. | Solvent extraction studies on cadmium: I. Extraction and separation of microamounts of cadmium halides in absence and presence of sulphuric acid | |
US381849A (en) | Teeeitoey | |
US2735752A (en) | Hydrazine recovery process | |
US541374A (en) | Risch | |
RU2580356C1 (en) | Method for heap leaching of gold from refractory ores | |
Bagnall et al. | Americyl (V) and americyl (VI) chloro-complexes | |
Sengupta et al. | Oxofluorovanadates (V). II Dioxodifluorovanadates | |
Spitsyn et al. | Present state of the chemistry of technetium | |
US3853353A (en) | Method of extracting a metal from a material containing the metal in elemental form | |
US1068730A (en) | Process of extracting values from ores. | |
Duisebayeva et al. | Prospects for use of chlorine-containing leaching solutions for extraction of associated useful components from spent ores of uranium deposits | |
US3689214A (en) | Process for the preparation of alkali metal trichromates me i cr308 | |
Muñoz-Ribadeneira et al. | Leaching of chalcopyrite (CuFeS2) with sodium chloride sulfuric acid solutions |