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    • 1. 发明申请
    • RECOVERY OF COBALT AND PGM METALS FROM COBALT ALLOYS CONTAINING PRECIOUS METALS BY SELECTIVE DISSOLUTION
    • 通过选择性溶解从含有重金属的钴合金中回收钴和PGM金属
    • WO2010076030A1
    • 2010-07-08
    • PCT/EP2009/009328
    • 2009-12-30
    • UMICOREOOSTERHOF, HaraldVLEUGELS, Eddy
    • OOSTERHOF, HaraldVLEUGELS, Eddy
    • C22B23/00C22B11/00C22B7/00C22B3/08C22B3/46C22B15/00
    • C22B11/046C22B3/08C22B3/46C22B7/007C22B11/048C22B15/0089C22B23/026C22B23/0461Y02P10/214Y02P10/22Y02P10/224Y02P10/234Y02P10/236
    • This disclosure concerns a process for the recovery of PGM from the cobalt-based, PGM-bearing alloys that are typically obtained after smelting spent GTL catalysts. The process comprises the steps of: - powdering the alloy to a mean particle size of less than 250 μm; - providing a mixed tank reactor equipped with means for feeding H 2 SO 4 and a CuSO 4 solution; - leaching in a mixed tank reactor the powdered alloy in a first acidic aqueous solution comprising H 2 SO 4 and CuSO 4 , thereby obtaining a CoSO 4 solution and a PGM-bearing metallic Cu residue; - isolating the PGM-bearing metallic Cu residue from the first CoSO 4 solution, by solid/liquid separation; - leaching in a mixed tank reactor the PGM-bearing metallic Cu residue in a second acidic aqueous solution comprising H 2 SO 4 and an oxidizing agent, thereby obtaining a CuSO 4 solution and a PGM concentrate; - isolating the PGM concentrate from the CuSO 4 solution, by solid/liquid separation; - returning the CuSO 4 solution to the step of leaching the powdered alloy. The main advantage of this process is that no H 2 is formed at any time, thus considerably enhancing the safety of the process compared to the classical acidic lixiviation of metallic compounds.
    • 本公开涉及从通常在熔化废GTL催化剂之后获得的基于钴的含PGM的合金中回收PGM的方法。 该方法包括以下步骤: - 将合金粉碎至平均粒度小于250μm; - 提供配备有用于供给H 2 SO 4和CuSO 4溶液的装置的混合罐式反应器; - 在混合罐式反应器中将粉末状合金浸入包含H 2 SO 4和CuSO 4的第一种酸性水溶液中,从而得到CoSO 4溶液和含PGM的金属Cu残余物; 通过固/液分离从第一种CoSO4溶液中分离含PGM的金属Cu残留物; - 在混合罐式反应器中将含有PGM的金属Cu残留物在包含H 2 SO 4和氧化剂的第二种酸性水溶液中浸出,从而得到CuSO 4溶液和PGM浓缩物; - 通过固/液分离从PGSO 4溶液中分离PGM浓缩物; - 将CuSO 4溶液返回到浸出粉末状合金的步骤。 该方法的主要优点是在任何时候都不形成H2,因此与经典的金属化合物的酸性浸出相比,显着提高了工艺的安全性。
    • 4. 发明申请
    • PROCESS FOR THE RECOVERY OF LITHIUM
    • 锂的回收工艺
    • WO2018082961A1
    • 2018-05-11
    • PCT/EP2017/077048
    • 2017-10-24
    • UMICORE
    • OOSTERHOF, HaraldDUPONT, David
    • C22B7/04C22B26/12
    • A process is divulged for the recovery of lithium from metallurgic slags comprising the steps of roasting spodumene to convert it from the alpha to the beta variant; reacting the beta variant with sulfuric acid, using a stoichiometric excess of acid; repulping the reaction product with water, forming an acidic slurry; neutralizing the acidic slurry to a pH between 5 and 7, by addition of at least one neutralizing agent; filtrating the neutralized slurry, thereby obtaining a lithium bearing solution and a residue; characterized that, in either one or both of the steps of repulping and neutralizing the acidic slurry, lithium-bearing metallurgic slag is added as neutralization agent. The lithium-bearing metallurgic slag is used to substitute at least part of the classic neutralizing agent. The lithium in the slag is released,and added to the lithium liberated from the spodumene.
    • 为了回收来自冶金炉渣的锂,公开了一种方法,其包括焙烧锂辉石以将其从α变为β变体的步骤; 使用化学计量过量的酸使β变体与硫酸反应; 用水再浆化反应产物,形成酸性浆液; 通过加入至少一种中和剂中和酸性浆液至pH值为5至7; 过滤中和的浆液,从而获得含锂溶液和残余物; 其特征在于,在酸化淤浆的再浆化和中和步骤中的任一个或两个步骤中,加入含锂冶金渣作为中和剂。 含锂冶金炉渣用于替代传统中和剂的至少一部分。 炉渣中的锂被释放出来,并添加到锂辉石中释放出的锂中。