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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。