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    • 2. 发明授权
    • Activated cathode and process for preparation thereof
    • 活性阴极及其制备方法
    • US06312571B1
    • 2001-11-06
    • US09511989
    • 2000-02-24
    • Miwako NaraMasashi TanakaYoshinori NishikiShuji Nakamatsu
    • Miwako NaraMasashi TanakaYoshinori NishikiShuji Nakamatsu
    • C25B900
    • C25B11/0484
    • An activated cathode comprising an electrically conductive substrate, an interlayer comprising a nickel oxide formed on the surface of the electrically conductive substrate, and a catalyst layer containing at least one lanthanum component selected from oxides and hydroxides of lanthanum metals and at least one platinum component selected from platinum metals and silver and oxides and hydroxides thereof formed on the interlayer. A process for the preparation of an activated cathode is also disclosed which comprises forming an interlayer comprising a nickel oxide on the surface of an electrically conductive substrate, and then forming a catalyst layer containing at least one lanthanum component selected from oxides and hydroxides of lanthanum metals and at least one platinum. component selected from platinum metals and silver and oxides and hydroxides thereof on the surface of the interlayer.
    • 包括导电基底的活化阴极,包含形成在导电基底表面上的氧化镍的中间层和包含至少一种镧组分的催化剂层,所述镧组分选自镧金属的氧化物和氢氧化物以及至少一种铂组分 由铂金属和银和其在中间层上形成的氧化物和氢氧化物组成。 还公开了一种制备活性阴极的方法,其包括在导电基材的表面上形成包含氧化镍的中间层,然后形成含有至少一种选自镧金属的氧化物和氢氧化物的镧组分的催化剂层 和至少一个铂。 组分选自铂金属和银,以及它们在中间层表面上的氧化物和氢氧化物。
    • 3. 发明授权
    • Electrolytic process and apparatus
    • 电解过程和设备
    • US6099914A
    • 2000-08-08
    • US401299
    • 1999-09-23
    • Yasuki YoshidaSetsuro OgataMasaharu UnoMasashi TanakaYoshinori NishikiTakayuki ShimamuneHiroshi InoueChiaki Iwakura
    • Yasuki YoshidaSetsuro OgataMasaharu UnoMasashi TanakaYoshinori NishikiTakayuki ShimamuneHiroshi InoueChiaki Iwakura
    • C01B3/00C23C18/16B05D1/18
    • C01B3/0078C10G45/00C10G45/32C25B1/02C25B3/00C10G2300/4056C10G2300/42Y02E60/324
    • An electrolytic process and apparatus which can operate in a hydrogen reaction chamber at a hydrogen reaction rate corresponding to the increase in the rate of production of hydrogen accompanying the increase in the electrolysis rate and maintain the current efficiency at a very high value with respect to the electrolytic current for producing hydrogen and a process for the production of an electrode for this purpose. An electrolytic process is provided which comprises effecting electrolysis of an electrolytic solution in an electrolytic chamber separated from a reaction chamber by a hydrogen-storing metal member with one surface of the hydrogen-storing metal member as a cathode opposing an anode so that hydrogen thus produced is adsorbed by the hydrogen-storing metal member while allowing hydrogen thus adsorbed and a material to be treated to undergo continuous catalytic reaction in the reaction chamber on the other surface of the hydrogen-storing metal member to cause hydrogenation or reduction reaction by hydrogen thus adsorbed, wherein an electrolytic apparatus having a porous catalyst layer provided on the catalytic reaction surface of the hydrogen-storing metal member is used. The porous catalyst layer is obtained by reducing metal cations in an electroless plating solution by active hydrogen desorbed from a hydrogen-storing metal so that the hydrogen-storing metal is plated with the metal.
    • 一种电解方法和装置,其可以在氢反应室中以氢反应速率操作,其伴随着电解速率的增加伴随着氢的生成速率的增加,并且将电流效率保持在非常高的值,相对于 用于生产氢的电解电流和用于生产电极的方法。 提供了一种电解方法,其包括通过储氢金属构件在与反应室分离的电解室中电解电解溶液,其中储氢金属构件的一个表面作为与阳极相对的阴极,从而产生氢 被吸氢金属部件吸附,同时允许被吸附的氢,并且被处理材料在储氢金属部件的另一个表面上的反应室中进行连续的催化反应,由此吸附氢气或还原反应 其中,使用具有设置在所述储氢金属构件的催化反应面上的多孔催化剂层的电解装置。 多孔催化剂层是通过从吸氢金属解吸的活性氢还原化学镀溶液中的金属阳离子而得到的,以使储氢金属镀金属。
    • 9. 发明授权
    • Electrolytic cell and method for the production of acid water
    • 电解池及酸水生产方法
    • US6126796A
    • 2000-10-03
    • US81059
    • 1998-05-19
    • Takayuki ShimamuneMasashi TanakaYasuo NakajimaYoshinori Nishiki
    • Takayuki ShimamuneMasashi TanakaYasuo NakajimaYoshinori Nishiki
    • C02F1/46C02F1/461C02F1/467
    • C02F1/4674C02F1/4618C02F2001/46133C02F2001/46161C02F2001/46185C02F2201/46115C02F2201/4618C02F2201/46185C02F2201/46195C02F2209/04C02F2209/06C02F2303/04
    • An electrolytic cell for the production of acid water which performs simple operation to produce acid water without complicated control over the concentration of hydrochloric acid to be added or precipitation of alkaline earth metal salts, which are disadvantages of the prior art electrolysis for the production of acid water. An electrolytic cell for the production of acid water, which comprises a power supply for applying a voltage across an anode chamber and a cathode chamber partitioned by an ion-exchange membrane. The anode in the anode chamber is disposed in close contact with the ion-exchange membrane. The electrolytic cell further comprises means for supplying an aqueous solution of hydrochloric acid and water to the cathode chamber and the anode chamber, respectively. Hydrochloric acid is not directly added to the anode chamber but indirectly added to the anode chamber by diffusing through the ion-exchange membrane. In this manner, hydrochloric acid is uniformly dispersed into the anode chamber by diffusing through the ion-exchange membrane. Thus, the need for controlling concentration is eliminated. Furthermore, because both the catholyte and anolyte are kept acidic, no precipitation of metal salts occurs.
    • 一种用于生产酸水的电解池,其操作简便,不需要对添加的盐酸的浓度进行复杂控制,或者沉淀碱土金属盐,这是现有技术电解生产酸的缺点 水。 一种用于生产酸水的电解池,包括用于施加跨越阳极室的电压的电源和由离子交换膜分隔的阴极室。 阳极室中的阳极设置成与离子交换膜紧密接触。 电解槽还包括用于将盐酸和水的水溶液分别供应到阴极室和阳极室的装置。 盐酸不直接添加到阳极室,而是通过离子交换膜扩散而间接添加到阳极室。 以这种方式,盐酸通过离子交换膜扩散而均匀地分散到阳极室中。 因此,消除了控制浓度的需要。 此外,由于阴极电解液和阳极电解液都保持酸性,因此不会发生金属盐沉淀。