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    • 1. 发明授权
    • Continuous process of converting non-ferrous metal sulfide concentrates
    • 连续加工有色金属硫化物浓缩物
    • US4266971A
    • 1981-05-12
    • US14521
    • 1979-02-23
    • Werner SchwartzPeter FischerHeinrich Traulsen
    • Werner SchwartzPeter FischerHeinrich Traulsen
    • C22B5/08C22B5/02C22B5/12C22B13/02C22B15/06C22B23/02C22B15/00
    • C22B5/02C22B5/12Y02P10/216
    • An improved continuous process for the conversion of a non-ferrous metal sulfide to form (A) a slag phase and (B) a non-ferrous metal phase of greater non-ferrous metal than the unconverted non-ferrous metal sulfide, by heating the non-ferrous metal sulfide in the form of a molten bath in a horizontal reactor provided with an oxidizing zone to which an oxidizing gas is added wherein in the oxidizing zone oxidation conditions predominate and a reducing zone to which a reducing gas is added and wherein in said reducing zone reducing conditions predominate is described. In the process, the slag is withdrawn from one end of the horizontal reactor while the non-ferrous metal phase is withdrawn from the other. In accordance with the invention, the gas atmosphere which develops in the horizontal reactor passes in counter-current flow to the flow of the slag phase and exhaust gas is withdrawn from the reactor at the same end of the reactor as is withdrawn the non-ferrous metal phase.
    • 通过加热有色金属硫化物以形成(A)渣相和(B)比未转化的有色金属硫化物更大的有色金属的有色金属相的改进的连续方法 在具有氧化气体的水平反应器中的熔融浴形式的有色金属硫化物,其中加入氧化气体,其中在氧化区域中氧化条件占优势,还原区域加入还原气体,其中在 描述了所述还原区还原条件占优势。 在此过程中,从水平反应器的一端抽出炉渣,而有色金属相从另一端取出。 根据本发明,在卧式反应器中形成的气体气氛通过逆流流向炉渣相的流动,并且排出的废气在反应器的同一端从反应器中排出,从而将有色金属 金属相。
    • 3. 发明授权
    • Continuous process of smelting metallic lead directly from lead-and
sulfur-containing materials
    • 直接从含铅和含硫材料冶炼金属铅的连续工艺
    • US4376649A
    • 1983-03-15
    • US275560
    • 1981-06-19
    • Werner SchwartzPeter Fischer
    • Werner SchwartzPeter Fischer
    • C22B13/06C22B13/02C22B13/08
    • C22B13/02C22B13/08
    • A molten bath consisting of a slag phase is maintained in an elongated horizontal reactor. The charge is fed into the reactor on one side thereof onto the molten bath in a melting zone so as to maintain an oxidation potential which causes metallic lead and slag to be formed. Reducing agent is introduced into the slag phase on the other side of the reactor in a reducing zone. To ensure that the bismuth contained in the charge is collected in the smallest possible quantity of crude lead, such an oxidation potential is maintained in the molten bath in the melting zone that the lead phase contains 0.05 to 2% by weight sulfur, the high-Bi primary lead which becomes available in that zone is separately tapped, and the low-Bi secondary lead which becomes available in the reducing zone is also separately tapped.
    • 由炉渣相组成的熔池保持在细长的水平反应器中。 电荷在其一侧的反应器中被送入熔融区的熔池中,以保持形成金属铅和熔渣的氧化电位。 将还原剂引入还原区的反应器另一侧的渣相中。 为了确保电荷中含有的铋以尽可能少的粗铅收集,在熔融区的熔池中保持氧化电位,铅相含有0.05〜2重量%的硫, 在该区域中可用的Bi主引线被分开抽头,并且在还原区域中变得可用的低Bi二次引线也被独立地分接。
    • 4. 发明授权
    • Continuous process of smelting metallic lead directly from lead- and
sulfur-containing materials
    • 直接从含铅和含硫材料冶炼金属铅的连续工艺
    • US4397688A
    • 1983-08-09
    • US271078
    • 1981-06-08
    • Werner SchwartzPeter Fischer
    • Werner SchwartzPeter Fischer
    • C22B5/02C22B13/02C22B13/06C22B15/00
    • C22B13/02
    • A slag phase and lead phase are conducted in a counter-current to each other in an elongated horizontal reactor, in which a gas atmosphere is conducted in a counter-current to the slag phase. To maintain the molten bath at a constant temperature and to permit an operation at the lowest possible temperatures whereby an undercooling of the melt is prevented, the temperature of the molten bath in the reducing zone is maintained constant by a controlled supply of additional heat, the temperature of the molten bath in the oxidizing zone is maintained constant by a control of the ratio of oxidizable sulfur to oxygen in such a manner that in case of a temperature rise the ratio of sulfur to oxygen is increased in order to decrease the lead oxide content of the slag and in case of a temperature drop of the ratio of sulfur to oxygen is decreased in order to increase the lead oxide content of the slag and the increase and decrease of the ratio of sulfur to oxygen are controlled allowing for the fact that the heat content of the gases entering the oxidizing zone from the reducing zone is changed with the lead oxide content of the slag.
    • 炉渣相和铅相在细长的水平反应器中以相反的方式进行,其中气体气氛以与炉渣相逆流的方式进行。 为了将熔浴保持在恒定温度并允许在最低可能的温度下进行操作,由此可以防止熔体的过冷,通过受控的额外的热量使还原区中的熔池的温度保持恒定, 通过控制可氧化硫与氧的比例,氧化区中的熔融液的温度保持恒定,使得在升高硫与氧的比率的情况下,为了降低氧化铅含量, 的炉渣,并且在硫与氧的比例的温度降低的情况下,为了增加炉渣的氧化铅含量而降低硫的比例,并且控制硫与氧的比例的增加和减少,这允许以下事实: 从还原区进入氧化区的气体的热含量随炉渣的氧化铅含量而变化。