首页> 外国专利> Brief description of the treatment of liquid effluents in a chloride medium and separation of the zinc and nickel, for its implementation and application to the industrial effluents metalliferous

Brief description of the treatment of liquid effluents in a chloride medium and separation of the zinc and nickel, for its implementation and application to the industrial effluents metalliferous

机译:氯化物介质中液体废水的处理以及锌和镍的分离的简要说明,以用于在含金属工业废水中的实施和应用

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。该罐包括:阴极室,该阴极室装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FR2977804B1

    专利类型

  • 公开/公告日2014-01-31

    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;C01G53;C01G9;

  • 国家 FR

  • 入库时间 2022-08-21 15:36:45

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