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    • 3. 发明申请
    • METHOD AND ARRANGEMENT FOR PRODUCING METAL POWDER
    • 生产金属粉末的方法和装置
    • WO2011092375A1
    • 2011-08-04
    • PCT/FI2011/050056
    • 2011-01-25
    • OUTOTEC OYJNIEMINEN, VilleVIRTANEN, Henri
    • NIEMINEN, VilleVIRTANEN, Henri
    • B22F9/24C25C1/00
    • C25C5/02B22F9/24C25B1/00
    • Method and arrangement for producing metal powder. In the method, dissolved utility metal is mixed in a solution containing at least one intermediary metal for precipitating the dissolved utility metal into a utility metal powder (14). In the method, the first part of an acid-containing starting solution is fed on the anode side (6) of an electrolytic cell as anolyte (1), to get in contact with the anode and the supply material containing yield metal, and the second part of the acid-containing starting solution, which also contains intermediary metal, is fed on the cathode side (8) of the electrolytic cell, to get in contact with the cathode (4) as catholyte (3); yield metal is oxidized and dissolved in the anolyte (1) by leading electric current in the anode (2); the yield metal contained in the second part of the starting solution is reduced on the cathode side (8); and anolyte solution and catholyte solution are fed in a precipitating chamber (12) for mixing the dissolved, oxidized yield metal and the second part of the starting solution containing reduced intermediary metal.
    • 生产金属粉末的方法和布置。 在该方法中,溶解的有用金属在含有至少一种中间金属的溶液中混合,用于将溶解的实用金属沉淀成金属粉末(14)。 在该方法中,将含酸的起始溶液的第一部分作为阳极电解液(1)供给到作为阳极电解液(1)的电解池的阳极侧(6),与阳极和含有收率金属的供给材料接触, 含有中间金属的含酸起始溶液的第二部分被供给到电解槽的阴极侧(8),以与阴极(4)作为阴极电解液(3)接触; 通过在阳极(2)中引导电流,产生的金属被氧化并溶解在阳极电解液(1)中; 包含在起始溶液的第二部分中的产量金属在阴极侧减少; 和阳极电解液和阴极电解质溶液进料到沉淀室(12)中,用于混合溶解的氧化产物金属和含有还原的中间金属的起始溶液的第二部分。
    • 4. 发明申请
    • METHOD OF ELECTROWINNING A METAL AND AN ELECTROLYSIS SYSTEM
    • 电镀金属和电解质体系的方法
    • WO2010089452A1
    • 2010-08-12
    • PCT/FI2010/050058
    • 2010-02-02
    • OUTOTEC OYJNIEMINEN, VilleVIRTANEN, Henri
    • NIEMINEN, VilleVIRTANEN, Henri
    • C25C7/06C25C7/04C25C1/08
    • C25C1/06C25C7/00C25C7/04
    • A method and a system of electrowinning, in an electrolytic tank, a metal from an electrolyte that contains a metallic salt. In the method, a diaphragm fabric is selected as the material of the anode bag from a group of diaphragm fabrics with different permeabilities, the dependences of the permeability of the diaphragm fabric on the viscosity of the catholyte and the pressure difference used are defined. On the basis of the defined dependences, the exit velocity of the anolyte from the anode bag is adjusted by the current density that is used, the pressure difference and the viscosity of the catholyte, so that an acid content of the anolyte of at least 50 g/1 is obtained. In the system, a fabric wherein the dependences of its permeability on the viscosity of the catholyte and the pressure difference used are known is selected as the diaphragm fabric of the anode bag from a group of diaphragm fabrics with different permeabilities. The exit velocity of the anolyte is adjusted by the current density used, the pressure difference and the viscosity of the catholyte, so that the acid content of the anolyte that is removed from the anode bag is at least 50 g/1.
    • 在电解槽中电解提取含有金属盐的电解质的金属的方法和系统。 在该方法中,从具有不同渗透性的隔膜织物组中选择隔膜织物作为阳极袋的材料,定义隔膜织物的渗透性对阴极电解液的粘度和使用的压差的依赖性。 基于确定的依赖性,阳极电解液从阳极袋的出口速度通过使用的电流密度,压力差和阴极电解液的粘度进行调节,使阳极电解液的酸含量至少为50 g / 1。 在该系统中,其渗透性对阴极电解液的粘度和所使用的压力差的依赖性已知的织物从具有不同渗透性的一组隔膜织物中选择为阳极袋的隔膜织物。 通过所使用的电流密度,阴极电解液的压力差和粘度来调节阳极电解液的出口速度,使得从阳极袋中除去的阳极电解液的酸含量为至少50g / l。