GB787296A - Improvements in or relating to removing impurities from platinum - Google Patents
Improvements in or relating to removing impurities from platinumInfo
- Publication number
- GB787296A GB787296A GB34917/55A GB3491755A GB787296A GB 787296 A GB787296 A GB 787296A GB 34917/55 A GB34917/55 A GB 34917/55A GB 3491755 A GB3491755 A GB 3491755A GB 787296 A GB787296 A GB 787296A
- Authority
- GB
- United Kingdom
- Prior art keywords
- platinum
- solution
- iron
- copper
- anion
- 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
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G55/00—Compounds of ruthenium, rhodium, palladium, osmium, iridium, or platinum
- C01G55/001—Preparation involving a liquid-liquid extraction, an adsorption or an ion-exchange
-
- 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
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/20—Treatment or purification of solutions, e.g. obtained by leaching
- C22B3/42—Treatment or purification of solutions, e.g. obtained by leaching by ion-exchange extraction
-
- 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
Abstract
Aqueous solutions containing platinum as part of a complex anion and also containing a cation impurity are purified by contacting the solution with a solid cation exchange material which absorbs the cationic impurity. The cation impurity may be copper, nickel, iron, manganese, magnesium, sodium or potassium. The platinum metal anion may be one containing F, Cl, Br, I, CN, NH2, NO or OH, for example chloroplatinic bromoplatinic, iodoplatinic fluoroplatinic, bromoplatinous, iodoplatinous, bromo-chloroplatinic, bromo-chloroplatinous, cyanoplatinic, aminoplatinic, nitrosoplatinic, hydroxyplatinic, the corresponding platinous acids or cyanochloropoplatinic, or hydroxy-chloroplatinic acid. The preferred cation exchangers are strongly acidic, such as sulfonated coal or carbonaceous zeolites orsynthetic resins of the phenolic or non-phenolic type, in particular a sulfonated copolymer of styrene and divinylbenzene. These materials may be employed as powders or chips or spheroids. The cation exchange material may be regenerated with an acid solution, and if a small amount of platinum is retained on the cation exchanger it may be removed with water washing and the solution so obtained may be contacted with an anion exchanger which picks up the platinum anion. The anion exchange material may then be burned to leave an ash of the platinum which may be taken up in water and re-purified. According to examples: (1) platinum containing minor percentages of iron and copper impurity were dissolved in aqua regia the solution evaporated to dryness and the resulting salt dissolved in distilled water. The solution was then again evaporated to dryness and the salt again dissolved in water and the resulting chloroplatinic acid solution containing the copper and iron impurities was passed through a bed of commercial "Amberlite" (Registered Trade Mark) cation exchange resin whereby the iron and copper impurities were retained. (2) Platinum containing iron and copper was dissolve in aqua regia as in Example (1) and the solution of chloroplatinic acid resulting was passed through a phenolic type cation exchange resin which freed the chloroplatinic acid from iron and copper impurities. The resin was then washed with distilled water to remove traces of platinum therefrom and the resulting solution contacted with an anion exchange resin of low ash content which picked up the platinum from the solution. The anion exchange material was then burned and the resulting platinum containing ash was dissolved in aqua regia and purified as before.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB34917/55A GB787296A (en) | 1955-12-06 | 1955-12-06 | Improvements in or relating to removing impurities from platinum |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB34917/55A GB787296A (en) | 1955-12-06 | 1955-12-06 | Improvements in or relating to removing impurities from platinum |
Publications (1)
Publication Number | Publication Date |
---|---|
GB787296A true GB787296A (en) | 1957-12-04 |
Family
ID=10371517
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB34917/55A Expired GB787296A (en) | 1955-12-06 | 1955-12-06 | Improvements in or relating to removing impurities from platinum |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB787296A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6024850A (en) * | 1993-10-27 | 2000-02-15 | Halox Technologies Corporation | Modified ion exchange materials |
US6402916B1 (en) | 1993-10-27 | 2002-06-11 | Richard L. Sampson | Electrolytic process and apparatus controlled regeneration of modified ion exchangers to purify aqueous solutions and adjust ph |
US10316388B2 (en) * | 2011-12-02 | 2019-06-11 | Stillwater Mining Company | Precious metals recovery |
-
1955
- 1955-12-06 GB GB34917/55A patent/GB787296A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6024850A (en) * | 1993-10-27 | 2000-02-15 | Halox Technologies Corporation | Modified ion exchange materials |
US6402916B1 (en) | 1993-10-27 | 2002-06-11 | Richard L. Sampson | Electrolytic process and apparatus controlled regeneration of modified ion exchangers to purify aqueous solutions and adjust ph |
US6416645B1 (en) | 1993-10-27 | 2002-07-09 | The State Of Connecticut, As Represented By The Department Of Economic And Community Development | Electrolytic process and apparatus for the controlled regeneration of modified ion exchangers to purify aqueous solutions |
US10316388B2 (en) * | 2011-12-02 | 2019-06-11 | Stillwater Mining Company | Precious metals recovery |
US11788170B2 (en) | 2011-12-02 | 2023-10-17 | Stillwater Mining Company | Precious metals recovery |
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