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    • 2. 发明公开
    • Process for producing electrolytic lead and elemental sulfur from galena
    • 一种用于从产生方铅矿电解铅和元素硫的过程。
    • EP0411687A2
    • 1991-02-06
    • EP90201909.0
    • 1990-07-13
    • B.U.S. ENGITEC SERVIZI AMBIENTALI S.r.l.
    • Olper, MarcoFracchia, Pierluigi
    • C25C1/18
    • C01B17/06C25C1/18Y02P10/212
    • The invention proposes a process for producing electrolytic lead and elemental sulfur from galena, characterized in that it comprises the following steps:

      (a) Galena is leached with an acidic aqueous solution of ferric fluoborate, with ferrous fluoborate, lead fluoborate and elemental sulfur being formed according to the reaction:
      2 Fe(BF₄)₃ + PbS → 2 Fe(BF₄)₂ + Pb(BF₄)₂ + S
      (b) the solid residue, composed by elemental sulfur and galena gangue is filtered off;
      (c) the solution of ferrous fluoborate and lead fluoborate coming from the (a) step is sent to a diaphragm electolytic cell, wherein pure lead is deposited at the cathode and at the anode ferrous ion is oxidated to ferric ion;
      (d) the solution of ferric fluoborate regenerated at the anode in said (c) step is recycled to said (a) step of galena leaching.

      By operating under suitable conditions, lead can be selectively dissolved and separated from the other metals small amounts of which are contained in galena together with said lead.
      Sulfur produced by the reaction can be separated from the gangue by extraction with a solvent, or by flotation.
    • 本发明提出了用于生产电解铅和从方铅矿元素硫,其特征在于在没有它包括以下步骤:(a)方铅矿在铁氟硼酸盐的酸性wässrige溶液中,用亚铁氟硼酸盐,铅氟硼酸盐和元素硫浸提而形成 gemäß到反应:2的Fe(BF 4)3 + PBS - > 2的Fe(BF 4)2 + PB(BF4)2 + S(b)该固体残余物,通过元素硫和方铅矿脉石组成的滤出; (C)氟硼酸亚铁和铅氟硼酸从步骤(a)来的溶液送到一个隔膜电解槽electolytic,worin纯铅在阴极和阳极处的亚铁离子被氧化成铁离子沉积; (D)氟硼酸铁在说步骤(c)在阳极再生的溶液再循环到所述(A)方铅矿浸出步骤。 通过在合适的条件下操作,铅可以被选择性地溶解并从少量这些都与铅包含在所述方铅矿一起其它金属分开。 由该反应产生的硫可从脉石通过萃取用溶剂通过浮选分离,或者。
    • 5. 发明公开
    • Process for continuous electrochemical lead refining
    • Verfahren zum fortlaufenden elektrochemischenLäuternvon Blei。
    • EP0638667A1
    • 1995-02-15
    • EP93202376.5
    • 1993-08-13
    • B.U.S. ENGITEC SERVIZI AMBIENTALI S.r.l.
    • Olper, Marco
    • C25C1/18
    • C25C1/18
    • The raw lead to be refined, whether of mineral origin or from reclaiming operations, the particle size of which has been reduced to a range not larger than 50 mm, is leached in a suitable apparatus with a solution of ferric fluoroborate in fluoroboric acid.
      During the leaching step, lead gets dissolved, with ferric fluoroborate being reduced to ferrous fluoroborate according to the following reaction:



              2 Fe (BF₄)₃ + Pb ---> Pb(BF₄)₂ + 2Fe(BF₄)   (1)



         The leaching apparatus behaves hence as an external anode installed outside of the cell.
      The resulting solution is sent to the cathodic compartment of a diaphragm cell in which lead is deposited on a cathode of stainless steel, in compact, highly pure form, from which it is periodically won.
      The so depleted-of-lead solution is sent to the anodic compartment of the same cell, in which a suitable anode oxidizes ferrous fluoroborate to ferric fluoroborate.
    • 无论矿物来源还是来自回收作业的原料铅在其合适的装置中用氟硼酸铁溶液在氟硼酸中浸出,将其粒度降至不大于50毫米的原料。 在浸出步骤中,铅溶解,氟铁酸根据以下反应还原为氟硼酸亚铁:2 Fe(BF4)3 + Pb ---> Pb(BF4)2 + 2Fe(BF4)(1>浸出 装置因此作为安装在电池外部的外部阳极,所得到的溶液被送到隔膜电池的阴极室,其中铅沉积在不锈钢的阴极上,呈紧密,高度纯净的形式,从该阴极室周期性地 将这样耗尽的铅溶液送到相同电池的阳极室,其中合适的阳极将氟硼酸亚铁氧化成氟硼酸铁。