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    • 3. 发明授权
    • Process for recovery by a solvent of the uranium present in phosphoric
acid
    • 通过磷酸中存在的铀溶剂回收的方法
    • US4643882A
    • 1987-02-17
    • US586288
    • 1984-03-05
    • Antoine Floreancig
    • Antoine Floreancig
    • C01B25/235C22B60/02C01G43/00C01B25/234
    • C01B25/235C22B60/026C22B60/0282
    • A process for the recovery of the uranium present in phosphoric acid produced by a wet process in (A) by means of a suitable solvent (L.sub.9), which is carried out after separation of the gypsum in (B) formed in the attack operation, and elimination of the solid materials which are still in suspension, characterized in that, in order to avoid the formation of dross in the course of the operation of extracting the uranium which is previously reduced in (D), the step of eliminating the solid materials which are still in suspension is effected by a final solid-liquid separation operation in (C) and/or in (E), prior to extraction of the uranium in (F), in the presence of an added fraction of gypsum (S.sub.22) and/or (S.sub.23) resulting from the production of H.sub.3 PO.sub.4.
    • 通过在(A)中通过在攻击操作中形成的(B)中分离石膏之后进行的合适的溶剂(L9)回收在(A)中通过湿法生产的磷酸中存在的磷酸的方法, 以及消除仍处于悬浮状态的固体材料,其特征在于为了避免在(D)中预先减少的铀萃取操作过程中形成浮渣,消除固体物质的步骤 在(F)中提取铀之前,在添加的石膏馏分(S22)的存在下,通过(C)和/或(E)中的最终固液分离操作, 和/或(S23)。
    • 4. 发明授权
    • Process for the selective separation of uranium and molybdenum which are
contained in an amino solvent
    • 包含在氨基溶剂中的选择性分离铀和钼的方法
    • US4381286A
    • 1983-04-26
    • US271941
    • 1981-06-09
    • Antoine Floreancig
    • Antoine Floreancig
    • C22B60/02C01G43/00C01G39/00
    • C22B60/026
    • The present invention relates to a process for the selective separation of uranium and molybdenum which are contained in an extract resulting from an amino solvent liquid-liquid extraction of a solution resulting from an attack on a molybdo-uraniferous ore by means of sulphuric acid, and which comprises re-extraction of the uranium in the presence of an oxidizing agent by means of an acid solution of an alkali metal chloride, followed by re-extraction of the molybdenum by means of an alkali metal carbonate solution. This process is characterized by using an oxidizing agent such as hydrogen peroxide, a small amount of which is added to the acid alkali metal chloride solution before the latter is brought into contact with the extract. This makes it possible to achieve selective separation of the uranium and molybdenum. This process can be used wherever molybdo-uraniferous ores are treated and where there is a requirement to produce a uranium concentrate which complies with the limits set in regard to the molybdenum content.
    • 本发明涉及一种选择性分离铀和钼的方法,所述方法包括在由通过硫酸对钼 - 铀矿矿进行的溶液的液 - 液萃取的氨基溶剂萃取物中提取的提取物中, 其包括在氧化剂存在下,通过碱金属氯化物的酸溶液重新萃取铀,然后通过碱金属碳酸盐溶液重新萃取钼。 该方法的特征在于使用氧化剂如过氧化氢,其中少量加入到酸性碱金属氯化物溶液中,然后使其与萃取物接触。 这使得可以实现铀和钼的选择性分离。 该方法可用于处理钼矿石矿石的地方,并且需要生产符合钼含量设定限值的铀浓缩物。
    • 7. 发明授权
    • Process for making into useful products the uranium and rare earths
contained in impure UF.sub.4 resulting from the extraction of uranium
from phosphoric acid
    • 制造有用产品的方法是从磷酸中提取铀所产生的不纯UF4中含有的铀和稀土
    • US4585626A
    • 1986-04-29
    • US516965
    • 1983-07-25
    • Antoine Floreancig
    • Antoine Floreancig
    • C01B15/047C22B60/02C01F13/00
    • C01B15/0475C22B60/0239C22B60/026
    • A process for making into useful products the uranium and rare earths contained in impure uranium tetrafluoride resulting from the recovery of uranium from phosphoric acid, comprising dissolving it in a hot condition in a nitric medium in the presence of an aluminum compound, treating the resulting solution with a solvent for extracting uranyl nitrate, which contains a phosphoric ester, and separating from the aqueous phase from which the uranium is removed, the solvent which is charged with uranyl nitrate to be made into a useful product, which provides that, in order to achieve easy separation of the aqueous phase from which the uranium has been removed, from the uranyl nitrate extraction solvent:(a) The operation of dissolution of UF.sub.4 is carried out in two steps at a suitable temperature, the first step comprising introducing insufficient amounts of nitric acid and the aluminum compound for complete dissolution of the impure uranium tetrafluoride and keeping the resulting suspension in an agitated condition for a period of time of at least 0.5 hour, and the second step comprising introducing amounts of nitric acid and the aluminum compound, which are at least sufficient to put into solution the uranium which was not dissolved in the first step, and while maintaining the suspension in an agitated condition; and(b) the uranyl nitrate is extracted by bringing into contact the aqueous medium resulting from the dissolution of UF.sub.4 and the uranyl nitrate extraction solvent containing the phosphoric ester.
    • 一种制备有用产物的方法,其中包含在从磷酸中回收铀所产生的不纯的四氟化铀中的铀和稀土,包括在铝化合物的存在下将其溶解在硝酸介质中的热条件下,将所得溶液 用用于提取含有磷酸酯的硝酸铀酰的溶剂,并从其中除去铀的水相中分离出溶剂,其中加入硝酸铀酰以制成有用的产物,其规定为了 从硝酸铀酰提取溶剂中实现容易地分离从其中除去铀的水相;(a)UF4的溶解操作在合适的温度下分两步进行,第一步包括引入不足量的 硝酸和铝化合物完全溶解不纯的四氟化铀,并保持所得的悬浮液 n处于搅拌条件下至少0.5小时的时间段,第二步骤包括将硝酸和铝化合物的量加入至少足以使溶解在第一步骤中不溶解的铀的溶液中 同时在悬浮状态下保持悬浮状态; 和(b)通过与UF4的溶解和含有磷酸酯的硝酸铀酰硝酸盐提取溶剂接触而引起的硝酸铀酰被提取。
    • 8. 发明授权
    • Process for extracting uranium from phosphoric acids by means of
alkylpyrophosphoric acids
    • 通过烷基吡咯烷酸从磷酸提取铀的方法
    • US4510122A
    • 1985-04-09
    • US511478
    • 1983-07-07
    • Antoine Floreancig
    • Antoine Floreancig
    • C22B60/02C01G43/00
    • C22B60/026
    • A process for extracting the uranium contained in phosphoric acid solutions by means of an extracting agent comprising an alkylpyrophosphoric acid, which comprises bringing into contact, in an agitated condition, the inorganic, phosphoric acid phase and an organic phase containing the extracting agent, thereby producing an emulsion, which is characterized in that, in an extraction unit comprising n stages in a cascade configuration, for each extraction stage, the emulsion is produced in a first step by simultaneously subjecting the two phases for a period of time T.sub.1 to an intense mechanical shearing action corresponding to a shearing coefficient of at least 5000 seconds.sup.-1 in order to multiply the contact surfaces for contact between said two phases, and then said emulsion in a second step is abruptly broke in a time T.sub.2, the sum of the times required for carrying out the two steps being at most 20 minutes.
    • 一种通过包含烷基焦磷酸的提取剂提取磷酸溶液中所含的铀的方法,其包括在搅拌条件下使无机磷酸相和含有萃取剂的有机相接触,由此产生 一种乳液,其特征在于,在包括级联构型的n级的萃取单元中,对于每个萃取阶段,在第一步中通过将两相经过一段时间T1同时进行强力机械 对应于至少5000秒-1的剪切系数的剪切动作,以便使所述两相之间的接触的接触面倍增,然后在第二步骤中的所述乳液在时间T2内突然断裂,所需时间的总和 执行两个步骤至多20分钟。