首页> 外国专利> Treating liquid effluent comprising zinc and nickel in solution in chloride medium, comprises conducting electrolysis of zinc and nickel solution in an electrolytic tank for dezincification and for nickel separation

Treating liquid effluent comprising zinc and nickel in solution in chloride medium, comprises conducting electrolysis of zinc and nickel solution in an electrolytic tank for dezincification and for nickel separation

机译:处理在氯化物介质中的溶液中包含锌和镍的液体流出物,包括在电解槽中进行锌和镍溶液的电解以脱锌和分离镍。

摘要

The process comprises conducting electrolysis of zinc and nickel solution in an electrolytic tank (1) for dezincification and for nickel separation. The tank comprises: a cathode chamber that is charged with the zinc and nickel solution as a catholyte and is equipped with a metal cathode (4), where zinc is deposited when the cathodic solution is dezincified and nickel is deposited; and an anode chamber that is charged in an acid medium such as sulfuric acid as an anolyte and is equipped with a anode (9). The cathode and anode chambers are separated by a cationic ion exchange membrane (6). The process comprises conducting electrolysis of zinc and nickel solution in an electrolytic tank (1) for dezincification and for nickel separation. The tank comprises: a cathode chamber that is charged with the zinc and nickel solution as a catholyte and is equipped with a metal cathode (4), where zinc is deposited when the cathodic solution is dezincified and nickel is deposited; and an anode chamber that is charged in an acid medium such as sulfuric acid as an anolyte and is equipped with a anode (9). The cathode and anode chambers are separated by a cationic ion exchange membrane (6). The effluent is pretreated by adding sulfuric acid and separating formed precipitate. The electrolytic tank for dezincification has pH value of 2+- 0.2. A potential of the cathode in the tank is -700 to -750 mV. A temperature at which the electrolysis is conducted in the electrolytic cell for dezincification is 20-30[deg] C. The electrolytic tank for nickel separation has pH value of 0.5+- 0.2. A potential of the cathode in the tank for nickel separation is -450 to -550 mV. A temperature at which the electrolysis is conducted in the electrolytic cell for nickel separation is 60-70[deg] C. An independent claim is included for an installation for treating liquid effluent.
机译:该方法包括在电解槽(1)中进行锌和镍溶液的电解,以进行脱锌和分离镍。所述罐包括:阴极室,其填充有作为阴极电解液的锌和镍溶液,并配备有金属阴极(4),当阴极溶液脱锌并沉积镍时,在其中沉积锌。阳极室,其填充在硫酸等酸性介质中作为阳极电解液,并具备阳极(9)。阴极室和阳极室被阳离子交换膜(6)隔开。该方法包括在电解槽(1)中进行锌和镍溶液的电解,以进行脱锌和分离镍。所述罐包括:阴极室,其填充有作为阴极电解液的锌和镍溶液,并配备有金属阴极(4),当阴极溶液脱锌并沉积镍时,在其中沉积锌。阳极室,其填充在硫酸等酸性介质中作为阳极电解液,并具备阳极(9)。阴极室和阳极室被阳离子交换膜(6)隔开。通过添加硫酸并分离形成的沉淀物来对流出物进行预处理。用于脱锌的电解槽的pH值为2±0.2。槽中阴极的电位为-700至-750 mV。在用于脱锌的电解池中进行电解的温度为20-30℃。用于镍分离的电解槽的pH值为0.5±0.2。槽中用于镍分离的阴极电位为-450至-550 mV。在用于分离镍的电解槽中进行电解的温度为60-70℃。包括独立权利要求用于处理液体流出物的设备。

著录项

  • 公开/公告号FR2977804A1

    专利类型

  • 公开/公告日2013-01-18

    原文格式PDF

  • 申请/专利权人 TREDI;

    申请/专利号FR20110056460

  • 申请日2011-07-15

  • 分类号B01D11/02;B01J39/08;C01G9;C01G53;

  • 国家 FR

  • 入库时间 2022-08-21 16:21:09

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