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    • 4. 发明申请
    • MONOPOLAR AND BIPOLAR ELECTROLYZER AND ELECTRODIC STRUCTURES THEREOF
    • MON阳和双极电解质及其电极结构
    • WO1986005216A1
    • 1986-09-12
    • PCT/EP1986000120
    • 1986-03-07
    • ORONZIO DE NORA IMPIANTI ELETTROCHIMICI S.P.A.DE NORA, Oronzio
    • ORONZIO DE NORA IMPIANTI ELETTROCHIMICI S.P.A.
    • C25B09/00
    • C25B9/206C25B9/20
    • Electrolyzer comprising at least an intermediate electrodic structure interposed between two electrodic end-structures, a separator on each side of said intermediate electrodic structure, means for impressing electrolysis current to the electrolyzer and means for feeding electrolytes to and withdrawing electrolysis products from the electrolyzer compartments. The intermediate electrodic structure comprises a current conducting and distributing core (1) of at least one highly conductive metal sheet; a series of substantially parallel, projecting ribs (2, 10) provided or not onto both surfaces of said core (1); a liner (3) on each side of the core (1) and made of a corrosion resistant metal. These liners (3) are formed by cold- or hot-pressing to fit to the ribs (2, 10) in case core ribs are provided, or have parallel ribs (10') fixed thereto in case core (1) has no ribs. Said liners (3) have peripheral projecting flanges (4) parallel to the liners.
    • 电解液至少包括插入在两个电极端部结构之间的中间电解质结构,在所述中间电解结构的每一侧上的隔板,用于向电解槽施加电解电流的装置,以及用于将电解质从电解槽隔室中提取并从其中取出电解产物的装置。 中间电解质结构包括至少一个高导电金属片的导电和分布芯(1); 在所述芯(1)的两个表面上设置或不设置的一系列基本上平行的突出的肋(2,10); 在芯部(1)的每一侧上具有由耐腐蚀金属制成的衬垫(3)。 这些衬垫(3)通过冷或热压形成,以便在提供芯肋的情况下配合肋(2,10),或者在芯(1)没有肋的情况下具有固定到其上的平行肋(10') 。 所述衬套(3)具有平行于衬套的周边突出凸缘(4)。
    • 6. 发明授权
    • Novel electrolyzer and process
    • 新型电解槽和工艺
    • US4417960A
    • 1983-11-29
    • US222958
    • 1981-01-06
    • Alberto Pellegri
    • Alberto Pellegri
    • C25B11/03C25B1/46C25B9/00C25B9/04C25B9/08C25B9/18C25B9/20C25B11/02C25B11/10C25B1/34
    • C25B9/04C25B9/206
    • A bipolar diaphragm or membrane electrolyzer comprising a housing containing an end anode element, an end cathode element and a plurality of bipolar elements with their major dimensions lying in a substantially vertical plane and comprised of a bipolar wall separating the anode compartment and the cathode compartment and vertical foraminous electrodes parallel positioned a certain distance from the bipolar wall, diaphragms or membranes separating the anodes and cathodes, a series of baffles distributed along the entire width of the electrode compartment and extending from the bipolar wall to the foraminous electrode to form a series of vertical flow channels extending over a large portion of the height of the wall, the said baffles being alternately inclined one way and the other way with respect to the vertical plane normal to the bipolar wall plane and spaced from one another whereby the ratio of the electrode surface intercepted by the edges of two baffles laterally defining a vertical flow channel to the flow section thereof is different from the ratio of the electrode surface intercepted by the edge of one of said two baffles and the edge of the adjacent baffle in the series and the flow section of the adjacent channel in the series to the said vertical flow channel, novel bipolar elements and improved methods of electrolysis.
    • 7. 发明授权
    • Deposition of catalytic electrodes on ion-exchange membranes
    • 在离子交换膜上沉积催化电极
    • US4364803A
    • 1982-12-21
    • US212173
    • 1980-12-02
    • Antonio NidolaGian N. Martelli
    • Antonio NidolaGian N. Martelli
    • B01J23/00B01J23/89B01J27/00C23C18/20C25B9/10C25B11/00C25B11/04C25D5/00C25D9/04C25D17/00
    • 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 the 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。
    • 8. 发明授权
    • Novel electrolysis cell
    • 新型电解槽
    • US4343689A
    • 1982-08-10
    • US57255
    • 1979-07-12
    • Oronzio de NoraPlacido M. Spaziante
    • Oronzio de NoraPlacido M. Spaziante
    • C25B11/02C25B1/24C25B1/46C25B9/00C25B9/08C25B9/18C25B9/20C25B11/03C25B13/00C25B1/26C25B11/00
    • C25B9/18C25B1/24C25B1/46C25B11/03C25B9/20
    • An electrolysis cell comprising a housing containing a plurality of alternating anode units and cathode units and an ion permeable membrane sheet disposed therebetween and having bonded to opposite sides of the membrane sheet a porous anode and a porous cathode, said cathode units comprising a pair of spaced foraminous electrical current cathode distributors of the same polarity forming a space for catholyte therebetween and means for flowing aqueous electrolyte through the catholyte space of the cathode unit and means for removing electrolysis products, the anode units comprising a pair of spaced foraminous electrical current anode distributors forming a space for anolyte therebetween, means for flowing aqueous halide solution through the said anolyte space and means for removing electrolysis products therefrom and means for uniformly compressing the units and membranes together whereby the current distributors are in firm electrical contact with their respective electrodes and to a novel method of generating halogens by electrolysis of aqueous halide solutions.
    • 一种电解槽,包括容纳多个交替阳极单元和阴极单元的壳体以及设置在其间的离子可渗透膜片,并且已经结合到膜片的相对侧,多孔阳极和多孔阴极,所述阴极单元包括一对间隔开的 具有相同极性的多孔电流阴极分配器形成用于阴极电解液的空间,以及用于使含水电解质流过阴极单元的阴极电解液空间的装置和用于去除电解产物的装置,阳极单元包括一对隔开的多孔电流阳极分配器, 其间用于阳极电解液的空间,用于使卤化物溶液流过所述阳极电解液空间的装置和用于从其中除去电解产物的装置,以及用于将单元和膜均匀压缩在一起的装置,由此电流分配器与其各自的电极牢固地电接触, 通过电解卤化物水溶液产生卤素的新方法。
    • 9. 发明授权
    • Electrolytic apparatus and process
    • 电解设备和工艺
    • US4263107A
    • 1981-04-21
    • US140137
    • 1980-04-14
    • Alberto Pellegri
    • Alberto Pellegri
    • C25B1/36C25B1/40C25B9/00C25B9/02C25B9/14C25B11/03
    • C25B11/03
    • Mass transfer to the surface of a substantially horizontal, foraminous gas-evolving electrode, suspended in the electrolyte pool over a co-operating electrode, is improved by inducing a vigorous multiple recirculation motion of the electrolyte to and from the interelectrodic gap through the openings in the foraminous electrode exploiting the gas lift of evolved gas bubbles by means of a multiplicity of baffles, alternatively slanting one way and the opposite with respect to the vertical axis, and defining, with their lower edges, an alternating series of large and small areas over the foraminous electrode surface; electrodes and cells incorporating the hydrodynamic means to effect recirculation are also disclosed.
    • 通过引起电解质通过开口处的电极间间隙的剧烈多次循环运动,将质子传递到悬浮在合作电极上的电解液池中的基本上水平的有孔气体放出电极的表面, 多孔电极通过多个挡板利用放出的气泡的气举,或者相对于垂直轴倾斜单向和相反,并且以它们的下边缘限定一系列交替的大小区域 有孔电极表面; 还公开了结合有流体动力装置来实现再循环的电极和电池。