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    • 44. 发明授权
    • Deposition of catalytic electrodes of ion-exchange membranes
    • 沉积离子交换膜催化电极
    • US4778578A
    • 1988-10-18
    • US122645
    • 1987-11-12
    • Antonio NidolaGian N. Martelli
    • Antonio NidolaGian N. Martelli
    • B01J23/00B01J23/89B01J27/00C23C18/20C25B9/10C25B11/00C25B11/04C25B1/00
    • C25B11/0478C23C18/2013C23C18/2033C23C18/208C25B11/00C25B9/10H01M2300/0082
    • A gas and electrolyte permeable metal layer is bonded to an ion-permeable membrane by electroless deposition to produce a permeable metal deposit upon the membrane or diaphragm. Advantageously, the membrane surface to be coated is pretreated with an amphoteric material. Thereafter, the treated surface is treated to deposit the coating. Typical metals deposited include platinum group metals, iron group metals, such as nickel, cobalt and others including gold and silver. The coatings are very thin, rarely in excess of about 50 to 100 microns.The coated membrane may be installed in an electrolytic cell used for producing chlorine and alkali by electrolysis of alkali metal chloride with the coating serving as one electrode and another opposed electrode on or adjacent to the opposite side of the membrane. It may also be used in water electrolysis and for other purposes.The coatings may be thickened by depositing other coatings of the same or different composition by suitable coating techniques.Especially adherent coatings are obtained when the metal deposited upon the pretreated surface is palladium metal or a mixture of palladium with another metal. Thickening coatings deposited upon such a porous palladium coating are found to have superior adherence and durability. The metal layer may be soaked or contacted with an alkali metal or an amalgam in presence of water to modify its crystal structure or grain size, if desired.
    • 通过无电沉积将气体和电解质渗透的金属层结合到离子可渗透膜,以在膜或膜片上产生可渗透的金属沉积物。 有利地,待涂覆的膜表面用两性材料预处理。 此后,处理表面被处理以沉积涂层。 沉积的典型金属包括铂族金属,铁族金属,如镍,钴等,包括金和银。 涂层非常薄,很少超过约50至100微米。 涂覆膜可以安装在用于通过电解碱金属氯化物而生产氯和碱的电解池中,其中涂层用作一个电极,而另一个相对的电极在膜的相对侧上或附近。 它也可用于水电解和其他目的。 通过合适的涂覆技术沉积相同或不同组成的其它涂层,可以使涂层变厚。 当沉积在预处理表面上的金属是钯金属或钯与另一种金属的混合物时,获得特别粘附的涂层。 发现沉积在这种多孔钯涂层上的增稠涂层具有优异的附着力和耐久性。 如果需要,金属层可以在水的存在下与碱金属或汞合金浸泡或接触以改变其晶体结构或晶粒尺寸。
    • 45. 发明授权
    • Electrolysis cell
    • 电解池
    • US4468311A
    • 1984-08-28
    • US382691
    • 1982-05-27
    • Oronzio de NoraAntonio NidolaGian N. Martelli
    • Oronzio de NoraAntonio NidolaGian N. Martelli
    • C25B9/00C25B1/46C25B9/04C25B9/08C25B9/10C25B11/02C25B13/08C25B11/03C25B11/12C25B15/08
    • C25B1/46C25B9/04C25B9/08
    • A cell is provided having an anode and cathode separated by an ion permeable membrane or diaphragm wherein an electrode layer is bonded to or otherwise embedded in on at least one and usually to both sides of the membrane. Polarity is imparted to a bonded or embedded electrode by pressing a crinkled resiliently compressible fabric against the membrane carrying the electrode layer. This fabric is substantially coextensive with the electrode layer and is constructed so that when compressed it exerts a substantially uniform elastic reaction pressure against the membrane carrying the electrode layer or a pliable foraminous sheet, i.e. screen, interposed between the membrane carrying the electrode layer and the resiliently compressible fabric. The resiliently compressible fabric has the ability of also transmitting pressure laterally so that pressure applied may distribute across the entire area of the layer and tendency to have local areas of too low of too high pressure is minimized or reduced.Chlorine or other halogen is produced by feeding an aqueous alkali metal halide or aqueous hydrogen halide to the anode chamber. Alkali is produced in the cathode chamber and withdrawn.
    • 提供具有由离子可渗透膜或隔膜隔开的阳极和阴极的电池,其中电极层与膜的至少一个并且通常到两侧结合或以其它方式嵌入在膜的至少一个并且通常到两侧。 通过将皱缩的弹性可压缩织物压靠在承载电极层的膜上而将粘合或嵌入电极赋予极性。 该织物与电极层基本上共同延伸,并且被构造成使得当被压缩时,其对承载电极层的膜或柔性多孔片(即屏幕)施加基本上均匀的弹性反应压力,所述膜介于带有电极层的膜和 弹性可压缩织物。 弹性可压缩织物具有横向传递压力的能力,使得施加的压力可以分布在层的整个区域上,并且具有太低压力的局部区域的最小化或减小的趋势。 氯或其它卤素通过将碱金属卤化物水溶液或卤水水溶液加入到阳极室来制备。 碱在阴极室中产生并被抽出。