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Extraktionsverfahren zur abtrennung von europium(III) und yttrium(III) aus luminophorenstaub und-schlamm

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    SYSNO ASEP0340911
    Document TypeP - Patent
    R&D Document TypePatent or other outcome protected by special legislation
    TitleExtraktionsverfahren zur abtrennung von europium(III) und yttrium(III) aus luminophorenstaub und-schlamm
    TitleMethod of Extraction of Europium(III) and/or Yttrium(III) Ions from Concentrate of Luminophore Dust or Sludge
    Author(s) Gruber, Václav (UCHP-M) RID, SAI
    Year of issue2009
    Possible third party use of the resultA - Pro využití výsledku jiným subjektem je vždy nutné nabytí licence
    Royalty requestedA - Poskytovatel licence požaduje licenční poplatek
    Patent no. or utility model no. or industrial design no.EP 1817437/AT E 426 684
    Date of the patent acceptance12.10.2009
    Name of the patent ownerÚstav chemických procesů AV ČR, v. v. i
    Current useA - Pouze udělený (dosud nevyužívaný) patent nebo patent využívaný jeho vlastníkem
    Languageger - German
    CountryAT - Austria
    Keywordsselective extraction ; recycling technologies ; ecological reprocessing
    Subject RIVCI - Industrial Chemistry, Chemical Engineering
    CEZAV0Z40720504 - UCHP-M (2005-2011)
    AnnotationDie Erfindung betrifft die selektive Isolierung von Yttrium- und Europium-Salzen aus dem Konzentrat von Luminophoren, welches mittels einer anorganischen Säure extrahiert wurde, bevorzugt mittels Salzäure oder Salpetersäure. Das Konzentrat der Luminophoren wird beim Recycling verwendetr Bildschirme von Farbfernsehgeräten oder Monitoren erhalten.
    Description in EnglishThe invention relates to a method of selective extraction of europium(III) and/or yttrium(III) from luminophore dust and sludge, the major components of which are oxides and sulphides of zinc, cadmium, yttrium and europium. From the concentrate of luminophore dust or sludge an aqueous solution is prepared and is subsequently contacted with an extraction agent, which is alkylphosphoric or dialkylphosphoric acid, either pure or diluted with organic solvent. The reaction equilibrium is strongly dependent on equilibrium concentration of the free acid in the aqueous phase of the reaction. After separating aqueous and organic phase after the extraction the europium(III) and yttrium(III) ions are recovered from the organic phase.
    WorkplaceInstitute of Chemical Process Fundamentals
    ContactEva Jirsová, jirsova@icpf.cas.cz, Tel.: 220 390 227
    Year of Publishing2010
Number of the records: 1  

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