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    • 31. 发明授权
    • Method of recovering uranium
    • 回收铀的方法
    • US4476099A
    • 1984-10-09
    • US219715
    • 1980-12-24
    • Floyd E. CampAmy B. Swartzlander
    • Floyd E. CampAmy B. Swartzlander
    • C22B60/02C01G43/00
    • C22B60/0282C22B60/026C22B60/0278
    • Uranium is recovered from a carbonate leach solution containing a dissolved uranium salt and a monovalent ion. The pH of the leach solution is adjusted to about 5 to about 7.5, and preferably to about 6 to about 7. Phosphate ion is then added to typical in-situ leach solutions in an amount from about 10 to about 30 mole % in excess of the amount needed to stoichiometrically react with the uranium in said solution. This results in the precipitation of a compound made up of the monovalent ion, uranium, and the phosphate ion, which is insoluble in the solution. The precipitate is then separated from the solution preferably by means of a centrifuge or a vortex clarifier. It can then be dissolved in acid, and the uranium extracted into an organic solvent such as DEHPA-TOPA in kerosene.
    • 从含有溶解的铀盐和一价离子的碳酸盐浸出液中回收铀。 将浸出溶液的pH调节至约5至约7.5,优选至约6至约7.然后将磷酸根离子加入到典型的原位浸提溶液中,其量为约10至约30摩尔%,超过 与所述溶液中的铀化学计量地反应所需的量。 这导致由不溶于溶液的一价离子,铀和磷酸根离子组成的化合物沉淀。 然后将沉淀物优选通过离心机或涡流澄清器从溶液中分离出来。 然后将其溶解在酸中,并将铀萃取到有机溶剂如DEHPA-TOPA中的煤油中。
    • 37. 发明授权
    • PROCESS FOR STRIPPING URANIUM FROM ALKYL PYROPHOSPHORIC ACID
    • 从碱性磷酸中分离铀的方法
    • US4428910A
    • 1984-01-31
    • US26747381
    • 1981-05-27
    • PRODECO INC
    • WORTHINGTON RALPH EMAGDICS ALEX
    • B01D11/04C01B25/238C01G20060101C01G43/00C22B60/02
    • C22B60/026Y02P10/212
    • A process is described for the recovery of tetravalent uranium from wet-process phosphoric acid utilizing an alkyl pyrophosphoric acid extractant or the like. After extracting the tetravalent uranium from wet-process acid, iron is stripped from the pregnant extractant into an oxalic acid stripping solution and then the tetravalent uranium is stripped from the pregnant extractant into an oxalate stripping solution. The oxalate stripping solution is an aqueous solution of an alkali metal or ammonium oxalate. The barren extractant is recycled for contacting with fresh wet-process acid. The uranium is oxidized and then precipitated in the oxalate stripping solution. The precipitated solids are separated from the solution, and the uranium is dried to a UO3 product.
    • 描述了使用烷基焦磷酸萃取剂等从湿法磷酸中回收四价铀的方法。 从湿法酸提取四价铀后,将铁从怀孕的萃取剂中剥离成草酸剥离溶液,然后将四价铀从怀孕的萃取剂中剥离成草酸溶液。 草酸盐剥离溶液是碱金属或草酸铵的水溶液。 贫瘠的萃取剂被再循环用于与新鲜的湿法酸接触。 铀被氧化,然后在草酸盐剥离溶液中沉淀。 将沉淀的固体与溶液分离,并将铀干燥成UO 3产物。
    • 38. 发明授权
    • Sequential process for extraction and recovery of vanadium and uranium
from wet process acids
    • 从湿法酸提取和回收钒和铀的顺序过程
    • US4427640A
    • 1984-01-24
    • US194444
    • 1980-10-06
    • P. David BowermanMichael F. Lucid
    • P. David BowermanMichael F. Lucid
    • C01G31/00C01G43/00C22B3/38C22B60/02
    • C01G43/00C01G31/003C22B3/0052C22B3/0091C22B60/026Y02P10/234
    • A process for preferentially extracting and recovering vanadium and uranium from wet process acids. The wet process acid first is contacted with a neutral organo-phosphorus compound to extract the vanadium values. The resulting loaded organic phase is separated from the wet process acid due to immiscibility of the acid and organic phases. The vanadium values then are separated from the organic phase by stripping. The raffinate separated from the first organic extractant then is contacted with a second organic extractant comprising a dialkylphosphoric acid and a neutral organo-phosphorus compound to extract the uranium values. The resulting loaded organic phase is separated from the wet process acid due to immiscibility of the acid and organic phases. The organic phase is stripped with a reductive stripping solution and the stripping solution then is oxidized to convert the uranium values to the hexavalent oxidation state. The oxidized solution then is contacted with another organic extractant to reextract the uranium to thereby concentrate the uranium product which then is stripped from the organic product with ammonium carbonate to form ammonium uranyl carbonate.
    • 从湿法酸中优先提取和回收钒和铀的方法。 首先将湿法酸与中性有机磷化合物接触以提取钒值。 由于酸和有机相的不混溶,所得负载的有机相与湿法酸分离。 然后通过汽提将钒值与有机相分离。 然后将与第一有机萃取剂分离的萃余液与包含二烷基磷酸和中性有机磷化合物的第二有机萃取剂接触以提取铀值。 由于酸和有机相的不混溶,所得负载的有机相与湿法酸分离。 有机相用还原汽提溶液汽提,然后将汽提溶液氧化,将铀值转化为六价氧化态。 然后将氧化溶液与另一种有机萃取剂接触以再提取铀,从而浓缩铀产物,然后用碳酸铵从有机产物中汽提出铀产物,形成碳酸铀酰铵。