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    • 46. 发明授权
    • Method for electrolyzing molten metal chlorides
    • 电解熔融金属氯化物的方法
    • US4192724A
    • 1980-03-11
    • US950111
    • 1978-10-10
    • Takeshi MinamiShinichi Toda
    • Takeshi MinamiShinichi Toda
    • C25B11/08C25C3/00C25C3/02C25C3/04C25C3/06C25C7/02
    • C25C7/025C25C3/00
    • A method for electrolyzing a molten chloride which comprises electrolyzing a molten bath of a chloride of a metal more base than hydrogen, such as sodium, magnesium, calcium or aluminum, in an electrolytic cell containing an anode and a cathode to form chlorine at the surface of the anode and the metal at the surface of the cathode,wherein the anode comprises an electrically conductive substrate resistant to corrosion by the molten bath of the metal chloride and the electrolysis products thereof and having thereon a coating of a noble metal oxide, andwith the electrolysis being carried out in the presence of an oxide or oxychloride of a metal more base than the metal formed at the cathode where the concentration of the oxide or oxychloride of the metal present in the molten bath, expressed as the mole fraction of free oxygen ion, is at least about 1.times.10.sup.-4.
    • 一种用于电解氯化氯的方法,其包括在含有阳极和阴极的电解池中电解比诸如钠,镁,钙或铝的氢更碱性金属的氯化物的熔池,以在表面形成氯 阳极和金属在阴极表面,其中阳极包括耐金属氯化物的熔池和其电解产物的腐蚀的导电基底,并且在其上具有贵金属氧化物的涂层,并且与 电解是在金属氧化物或氯氧化物的存在下进行的,其金属比在阴极处形成的金属更碱,其中存在于熔池中的金属的氧化物或氯氧化物的浓度以游离氧的摩尔分数表示 离子,至少约1×10 -4。
    • 48. 发明授权
    • Coated titanium anode for amalgam heavy duty cells
    • 用于汞合金重载电池的涂层钛阳极
    • US4022679A
    • 1977-05-10
    • US642384
    • 1975-12-19
    • Konrad KoziolKarl-Heinz SiebererBaptist Zenk
    • Konrad KoziolKarl-Heinz SiebererBaptist Zenk
    • C25B11/02C25B11/08C25B11/10
    • C25B11/02
    • The anode is particularly designed for use at anodic densities D.sub.A greater than 10 kA/m.sup.2, and comprises substantially horizontally extending coated anode segments having a clear spacing of at least 1.5 mm from each other and upwardly extending lateral surfaces. Each segment has an active coated part higher than 5 mm and not exceeding 20 mm, measured from the horizontal undersurface of the anode. The actual active surface of the parts, up to heights of 5 mm, 7.5 mm, 10 mm and 15 mm, respectively, exceeds at least 2.5, 3.33, 4 and 4.7 times, respectively, the projected anode area which latter is the total area bounded by the periphery of the anode. At least half the actual active surface extends upwardly relative to the horizontal base area of the anode.
    • 阳极特别设计用于大于10kA / m 2的阳极密度DA,并且包括基本上水平延伸的涂覆阳极段,其具有彼此至少1.5mm的清晰间隔和向上延伸的侧表面。 每个段具有从阳极的水平下表面测量的高于5mm且不超过20mm的活性涂层部分。 部件的实际有效表面分别高达5 mm,7.5 mm,10 mm和15 mm的高度,分别超过投影阳极面积的2.5,3.3,4.4和4.7倍,后者是总面积 由阳极的周边界定。 实际活性表面的至少一半相对于阳极的水平基底区域向上延伸。