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    • 1. 发明授权
    • Purifying mixed-cation electrolyte
    • 净化混合阳离子电解质
    • US4670116A
    • 1987-06-02
    • US844153
    • 1986-03-26
    • Francis GoodridgeRaymond E. PlimleyRobert P. Leetham
    • Francis GoodridgeRaymond E. PlimleyRobert P. Leetham
    • C25C1/00C25C1/16C25D21/18C25F5/00
    • C25D21/18C25C1/00C25C1/16
    • An electrolyte containing 65 g/l zinc and 150 g/l Cu is purified in zinc, that is, the copper is removed, by causing the electrolyte to fluidize a bed 8 of 1/2 mm copper particles. The bed is fluidized by 25% to make it 42 cm deep. An anode 11 is disposed above the top of the bed. A cathode 9 is disposed part-way up the bed. Copper is electroplated onto the bed particles. Any zinc which may be electroplated onto the bed particles tends to redissolve with concomitant cementation, on the particles, of copper, which can be recovered. The electrolyte is thus eventually completely stripped of copper and can be used for zinc electrowinning.By controlling the pH of the electrolyte, substantially one metal, or one desired combination of metals, may be removed. In particular, pure copper deposition can be completed at low pH even in the presence of cadmium; upon a substantial increase in pH, cadmium deposition will occur.
    • 在锌中纯化含有65g / l锌和150g / l Cu的电解质,即通过使电解液使1/2的铜颗粒床8流化,除去铜。 床层流动25%,使其达到42厘米深。 阳极11设置在床的顶部上方。 阴极9被布置在床的一部分上。 将铜电镀到床颗粒上。 任何可能电镀在床颗粒上的锌,往往会随着附着的胶结而重新溶解在可以回收的铜颗粒上。 因此,电解质最终完全被铜剥离,并可用于锌电解提取。 通过控制电解质的pH,可以除去基本上一种金属或一种所需的金属组合。 特别是即使在镉存在下,也可以在低pH下完成纯铜沉积; 在pH的显着增加时,将发生镉沉积。
    • 2. 发明授权
    • Electrochemical processes
    • 电化学工艺
    • US4124453A
    • 1978-11-07
    • US617489
    • 1975-09-29
    • Martin FleischmannFrancis GoodridgeChristopher J. H. King
    • Martin FleischmannFrancis GoodridgeChristopher J. H. King
    • C25B1/00C25B1/24C25B3/10B01K1/00
    • C25B3/10C25B1/00C25B1/24
    • A method of carrying out an electrochemical reaction comprises setting up a fluidized bed of particles at least some of which have at least their surfaces conducting or semi-conducting, using upwardly flowing liquid electrolyte, with or without reactant liquid, for the purpose, and applying a voltage gradient across at least a portion of said fluidized bed of particles, the size of particles, the conductivity of and rate of flow of the said electrolyte and/or reactant liquid and the voltage gradient being such that not only are anodic and cathodic faces established in respect of each of some of the at least partly conducting particles but the electropotentials on said faces on substantially each bipolar particle are such that said electrochemical reaction takes place on at least some of said bipolar particles but only on one portion of the surfaces thereon of said particles. The said bipolar particles which, preferably, are spherical or cylindrical may comprise solid conducting or semi-conducting material or cores of non-conducting material with coatings of conducting or non-conducting material thereon.The said method may be, for example, the electrolysis of sea water for the production of hypochlorite or of bromide solution for the production of hypobromite or the decarboxylation of monomethyl adipate to dimethyl sebacate.
    • 进行电化学反应的方法包括使用向上流动的液体电解质,至少其中一些具有至少其表面导电或半导电的颗粒的流化床,用于或不使用反应物液体,并施加 在所述流化床颗粒的至少一部分上的电压梯度,所述电解质和/或反应液体的粒子尺寸,电导率和流速以及电压梯度不仅是阳极和阴极面 建立在每个至少部分导电颗粒中的每一个上,但是基本上每个双极性颗粒上的所述表面上的电位使得所述电化学反应发生在至少一些所述双极性颗粒上,但仅在其上的一部分表面上 的所述颗粒。 所述优选为球形或圆柱形的双极性颗粒可包括其上具有导电材料或非导电材料的非导电材料的固体导电或半导电材料或芯。
    • 9. 发明授权
    • Electrochemical cell and process
    • 电化学电池和工艺
    • US4270995A
    • 1981-06-02
    • US57489
    • 1979-07-13
    • Francis GoodridgeRaymond E. Plimley
    • Francis GoodridgeRaymond E. Plimley
    • C25B3/02C25B9/06C25B9/18C25B3/06C25B9/00C25B15/08
    • C25B9/066C25B3/02C25B9/063C25B9/18
    • An electrochemical cell comprises a housing (1,2) divided by a perforated generally horizontal plate (3) into an upper chamber (4) and a lower chamber (5). Bipolar electrodes (19, 21) are disposed in the upper chamber (4) above perforations (23) in the plate (3), between electrolyte inlet and outlet weirs (11, 13) for flowing electrolyte over the plate (3). The lower chamber (5) is a gas-supply chamber for passing a gas, e.g. propylene, up through the perforations (23), so as to bubble the gas through electrolyte (e.g. NaBr solution) on the plate (3) and into the upper gas-collection chamber (4). A reactor may be formed by stacking several cells with their electrolyte flows in cascade. The cell is particularly suitable for electro-organic syntheses involving a gaseous reactant.
    • 电化学电池包括由穿孔的大体水平板(3)分成上室(4)和下室(5)的壳体(1,2)。 双极电极(19,21)设置在板(3)中的穿孔(23)上方的上室(4)中,用于将电解液流过板(3)的电解质入口和出口堰(11,13)之间。 下室(5)是用于使气体通过的气体供给室, 丙烯,通过穿孔(23)向上,以使气体通过板(3)上的电解质(例如NaBr溶液)气泡并进入上部气体收集室(4)。 反应器可以通过层叠多个电池与其电解质流而形成。 该电池特别适用于涉及气态反应物的电 - 有机合成。