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    • 5. 发明授权
    • Rare earth recovery from phosphor
    • 稀土从磷光体回收
    • US08524176B2
    • 2013-09-03
    • US13714276
    • 2012-12-13
    • REEnewal Corporation
    • Narayan V. Thakur
    • C01F17/00
    • C22B59/00C01F17/0006C01F17/0043C01P2006/80
    • A method is described to produce high purity rare earth oxides of the elements La, Ce, Tb, Eu and Y from phosphor, such as waste phosphor powders originating in various consumer products. One approach involves leaching the powder in two stages and converting to two groups of relatively high purity mixed rare earth oxides. The first group containing Eu and Y is initially separated by solvent extraction. Once separated, Eu is purified using Zn reduction with custom apparatus. Y is purified by running another solvent extraction process using tricaprylmethylammonium chloride. Ce is separated from the second group of oxides, containing La, Ce and Tb by using solvent extraction. Subsequently, La and Tb are separated from each other and converted to pure oxides by using solvent extraction processes. A one-stage leaching process, wherein all rare earths get leached into the solution and subsequently processed, is also described.
    • 描述了一种从磷光体中产生元素La,Ce,Tb,Eu和Y的高纯度稀土氧化物的方法,例如源自各种消费品的废磷粉末。 一种方法是将粉末分两个阶段浸出并转化成两组相对较高纯度的混合稀土氧化物。 含有Eu和Y的第一组最初通过溶剂萃取分离。 一旦分离,使用定制装置使用Zn还原来纯化Eu。 通过使用三氯丙基甲基氯化铵进行另一种溶剂萃取方法纯化Y。 通过溶剂萃取,Ce与含有La,Ce和Tb的第二组氧化物分离。 随后,通过使用溶剂萃取方法将La和Tb彼此分离并转化为纯氧化物。 还描述了一阶段浸出方法,其中所有稀土被浸出到溶液中并随后被处理。
    • 6. 发明授权
    • Methods of recovering rare earth elements
    • 回收稀土元素的方法
    • US08216532B1
    • 2012-07-10
    • US13163325
    • 2011-06-17
    • Albert A. Vierheilig
    • Albert A. Vierheilig
    • C01G17/00
    • B01J29/06B01J20/186B01J20/3408B01J20/345B01J29/061B01J29/90B01J38/02B01J38/60B01J38/68C01F17/00C01F17/0006C22B7/006C22B59/00Y02P10/234Y02P10/236Y02P20/584
    • Processes described include reacting a fresh or spent catalyst, or sorbent, with a solution containing an extracting agent (such as an acid or a base). Preferably, the catalyst contains both alumina and a molecular sieve (or a sorbent), and the reaction is performed under relatively mild conditions such that the majority of the base material does not dissolve into the solution. Thus, the catalyst can be re-used, and in certain instances the performance of the catalyst even improves, with or without re-incorporating certain of the metals back into the catalyst. Additionally, metals contained in the catalyst, such as Na, Mg, Al, P, S, Cl, K, Ca, V, Fe, Ni, Cu, Zn, Sr, Zn Sb, Ba, La, Ce, Pr, Nd, Pb, or their equivalent oxides, can be removed from the catalyst. Some of the metals that are removed are relatively valuable (such as the rare earth elements of La, Ce, Pr and Nd).
    • 所述方法包括使新鲜或废催化剂或吸附剂与含有萃取剂(例如酸或碱)的溶液反应。 优选地,催化剂含有氧化铝和分子筛(或吸附剂),反应在相对温和的条件下进行,使得大部分基材不溶解于溶液中。 因此,可以重新使用催化剂,并且在某些情况下催化剂的性能甚至改善,有或没有将某些金属重新引入催化剂。 另外,催化剂中所含的金属如Na,Mg,Al,P,S,Cl,K,Ca,V,Fe,Ni,Cu,Zn,Sr,Zn Sb,Ba,La,Ce,Pr,Nd ,Pb或其等价氧化物可以从催化剂中除去。 被去除的一些金属是相对有价值的(例如La,Ce,Pr和Nd的稀土元素)。
    • 7. 发明授权
    • Actinide extraction methods
    • 锕系提取方法
    • US07799293B2
    • 2010-09-21
    • US11530508
    • 2006-09-11
    • Dean R. PetermanJohn R. KlaehnMason K. HarrupRichard D. TillotsonJack D. Law
    • Dean R. PetermanJohn R. KlaehnMason K. HarrupRichard D. TillotsonJack D. Law
    • B01D11/04C01G56/00C22B60/00
    • C01G56/001C01F17/0006C07F9/304C22B3/007C22B59/00Y02P10/234
    • Methods of separating actinides from lanthanides are disclosed. A regio-specific/stereo-specific dithiophosphinic acid having organic moieties is provided in an organic solvent that is then contacted with an acidic medium containing an actinide and a lanthanide. The method can extend to separating actinides from one another. Actinides are extracted as a complex with the dithiophosphinic acid. Separation compositions include an aqueous phase, an organic phase, dithiophosphinic acid, and at least one actinide. The compositions may include additional actinides and/or lanthanides. A method of producing a dithiophosphinic acid comprising at least two organic moieties selected from aromatics and alkyls, each moiety having at least one functional group is also disclosed. A source of sulfur is reacted with a halophosphine. An ammonium salt of the dithiophosphinic acid product is precipitated out of the reaction mixture. The precipitated salt is dissolved in ether. The ether is removed to yield the dithiophosphinic acid.
    • 公开了从镧系元素分离锕系元素的方法。 在有机溶剂中提供具有有机部分的区域特异性/立体特异性二硫代次膦酸,然后与含有锕系元素和镧系元素的酸性介质接触。 该方法可以延伸到彼此分离锕系元素。 提取锕系元素作为与二硫代次膦酸的络合物。 分离组合物包括水相,有机相,二硫代次膦酸和至少一种锕系元素。 组合物可以包括另外的锕系元素和/或镧系元素。 还公开了包含至少两个选自芳族化合物和烷基的有机部分的二硫代次膦酸的方法,每个部分具有至少一个官能团。 硫源与卤代膦反应。 二硫代次膦酸产物的铵盐从反应混合物中沉淀出来。 将沉淀的盐溶于乙醚中。 除去乙醚,得到二硫代次膦酸。