GB787296A - Improvements in or relating to removing impurities from platinum - Google Patents

Improvements in or relating to removing impurities from platinum

Info

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
Application number
GB34917/55A
Inventor
Herbert Rudolph Appell
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Universal Oil Products Co
Original Assignee
Universal Oil Products Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Universal Oil Products Co filed Critical Universal Oil Products Co
Priority to GB34917/55A priority Critical patent/GB787296A/en
Publication of GB787296A publication Critical patent/GB787296A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G55/00Compounds of ruthenium, rhodium, palladium, osmium, iridium, or platinum
    • C01G55/001Preparation involving a liquid-liquid extraction, an adsorption or an ion-exchange
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/42Treatment or purification of solutions, e.g. obtained by leaching by ion-exchange extraction
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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.
GB34917/55A 1955-12-06 1955-12-06 Improvements in or relating to removing impurities from platinum Expired GB787296A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (5)

* Cited by examiner, † Cited by third party
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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