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    • 1. 发明授权
    • Solvent extraction of gallium from acidic solutions containing phosphorus
    • 从含磷的酸性溶液中提取镓
    • US5221525A
    • 1993-06-22
    • US821764
    • 1992-01-14
    • James A. BradburyMichael E. ColemanSusan D. Roberts
    • James A. BradburyMichael E. ColemanSusan D. Roberts
    • C01G15/00
    • C01G15/003Y10S423/14
    • A process for extracting gallium from an aqueous gallium-bearing acidic solution comprises: a) providing a quantity of phosphorus within the aqueous gallium-bearing solution, the phosphorus being provided in an aqueous soluble form and being substantially dissolved within the aqueous solution, the aqueous gallium-bearing solution having dissolved phosphorus defining a first aqueous phase; b) intermixing the aqueous gallium-bearing solution having the quantity of aqueous soluble dissolved phosphorus with a first organic phase comprising a quantity of an alkylated 8-hydroxyquinoline; c) separating the intermixed first aqueous phase and first organic phases into a second aqueous phase and a second organic phase, the quantities of aqueous soluble phosphorus and alkylated 8-hydroxyquinoline being effective to extract gallium from the aqueous gallium-bearing solution to provide a gallium concentration in the second organic phase which is greater than a gallium concentration in the first organic phase and to provide a gallium concentration in the second aqueous phase which is less than a gallium concentration in the first aqueous phase, the gallium concentration in the second organic phase being greater than if no aqueous soluble phosphorus were present in the first aqueous solution; and d) stripping gallium from the second organic phase with an acid solution.
    • 从含镓含水酸性溶液中提取镓的方法包括:a)在含水镓水溶液中提供一定量的磷,磷以水溶性形式提供并基本上溶解在水溶液中,水溶液 具有限定第一水相的溶解磷的含镓溶液; b)将具有一定量的水溶性溶解磷的含水含水溶液与包含一定数量的烷基化8-羟基喹啉的第一有机相混合; c)将混合的第一水相和第一有机相分离成第二水相和第二有机相,水溶性磷和烷基化8-羟基喹啉的量有效地从含水镓水溶液中提取镓,以提供镓 在第二有机相中的浓度大于第一有机相中的镓浓度,并且在第二水相中提供小于第一水相中的镓浓度的镓浓度,第二有机相中的镓浓度 大于在第一水溶液中不存在水溶性磷的情况; 和d)用酸溶液从第二有机相中除去镓。
    • 3. 发明授权
    • Recovery of cobalt values
    • 回收钴价值
    • US4261737A
    • 1981-04-14
    • US89837
    • 1979-10-31
    • James A. BradburyRichard T. Um
    • James A. BradburyRichard T. Um
    • C22B15/00B01D15/00C22B20060101C22B1/00C22B3/00C22B3/24C22B7/00C22B23/00C22B47/00C22B23/04
    • C22B3/24Y02P10/234
    • The present process involves an improvement in the hydrometallurgical recovery of metal values from metal bearing sources such as ores and the like. The desired metal values are recovered by subjecting a metal bearing source to a reductive roast in a reducing atmosphere after having treated said source with at least one additive. Following the reductive roast the reduced metal bearing source is cooled and extracted by a leaching operation. The separation of various metal values in the metal bearing source may be effected by adding a solid adsorbent to the leach solution whereby selective metal ions are adsorbed thereon. The improvement in the present process comprises pretreating the solid adsorbent prior to use thereof with an acid thereby increasing the loading capacity of the metal ions in the adsorbents as well as kinetics of metal adsorption.
    • 本发明的方法涉及从诸如矿石等金属轴承来源改进金属值的湿法冶金回收。 在用至少一种添加剂处理所述源之后,通过使金属轴承源在还原性气氛中经受还原性焙烧来回收所需的金属值。 还原烘烤后,还原金属轴承源被冷却并通过浸出操作提取。 金属轴承源中各种金属值的分离可以通过向浸出溶液中加入固体吸附剂来实现,其中选择性金属离子被吸附在其上。 本方法的改进包括在使用之前用酸预处理固体吸附剂,从而增加吸附剂中金属离子的负载能力以及金属吸附的动力学。