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    • 91. 发明授权
    • Cell and process for electrolyzing aqueous solutions using a porous
anode separator
    • 使用多孔阳极分离器电解水溶液的电池和方法
    • US4140615A
    • 1979-02-20
    • US782117
    • 1977-03-28
    • Igor V. KadijaByung K. Ahn
    • Igor V. KadijaByung K. Ahn
    • C25B1/46C25B9/08C25B11/04C25B9/00
    • C25B11/0478C25B1/46C25B9/08
    • Electrolysis of alkali metal chloride solutions to produce chlorine and alkali metal hydroxides is accomplished in a cell comprising an anode compartment, a cathode compartment, a cation permeable divider separating the anode compartment from the cathode compartment, where the anode compartment contains an anode separator. The anode separator is comprised of a porous plate of a valve metal having an electrochemically active coating on the face, and an electrochemically non-active barrier layer on the back and a portion of the interior. The anode separator is positioned in the anode compartment so that the back of the anode separator is spaced apart from the cation permeable divider. An alkaline brine zone is formed between the anode separator and the cation permeable divider which increases the service life of the cation permeable divider. In addition, the anode separator provides improved chlorine gas separation properties, increased service life for the electroconductive coating on the face, and enables the cell to operate with a reduced cell voltage.
    • 电解碱金属氯化物溶液以产生氯和碱金属氢氧化物在包括阳极室,阴极隔室,将阳极室与阴极隔室分隔开的阳离子可渗透隔板的电池中完成,其中阳极室包含阳极隔板。 阳极分离器包括具有在表面上具有电化学活性涂层的阀金属的多孔板,以及背面和内部的一部分上的电化学非活性阻挡层。 阳极分离器位于阳极室中,使得阳极分离器的背面与阳离子可渗透分隔器间隔开。 在阳极分离器和阳离子可渗透分隔器之间形成碱性盐水区,这增加了阳离子可渗透分隔器的使用寿命。 此外,阳极隔板提供改善的氯气分离性能,增加了表面上的导电涂层的使用寿命,并且使电池能够以降低的电池电压工作。
    • 97. 发明授权
    • Process for the electrolytic treatment of alkali halide
    • 碱卤化物电解处理方法
    • US4076604A
    • 1978-02-28
    • US732095
    • 1976-10-13
    • Naohiro MurayamaKenichi NakamuraMakoto FukudaTeruo SakagamiShirou Suzuki
    • Naohiro MurayamaKenichi NakamuraMakoto FukudaTeruo SakagamiShirou Suzuki
    • C25B1/46C25B1/16C25B1/26
    • C25B1/46
    • In an electrolytic treatment of alkali halide for the manufacture of alkali hydroxide, a three-chamber type reaction vessel assembly is used so as to provide an anodic chamber, an intermediate chamber and a cathodic chamber arranged in succession one after another and mutually separated by means of anodic (i.e., cationic selective) ion exchange membranes. From the intermediate chamber, low concentration caustic alkali solution is obtained, while from the cathodic chamber, high concentration caustic alkali solution is obtained. In this electrolytic process, the system is operated with the cathodic chamber supplied with no water or aqueous content. The high concentration caustic alkali solution is made from water and alkali metal ions conveyed from the intermediate chamber to the cathodic chamber and exclusively and osmotically passed through the anodic ion exchange membrane. The polymers or copolymers of the anodic ion exhange membrane include sulfonic acid, carboxylic acid and/or phenolic radicals. As the method for the introduction of these radicals, formation of corresponding copolymers may be utilized in the most recommended way. As an example, the membrane may comprise a fluorinated polymer having a cyclic ring structure unit and pendant type sulfonic acid radicals.
    • 在用于制造碱金属氢氧化物的碱金属卤化物的电解处理中,使用三室式反应容器组件,以便提供一个接一个地连续排列并相互分离的阳极室,中间室和阴极室 的阳极(即阳离子选择性)离子交换膜。 从中间室获得低浓度苛性碱溶液,而从阴极室获得高浓度苛性碱溶液。 在这种电解过程中,系统在没有水或含水量的阴极室运行。 高浓度苛性碱溶液由从中间室输送到阴极室的水和碱金属离子制成,并且渗透通过阳极离子交换膜。 阳离子离子膜的聚合物或共聚物包括磺酸,羧酸和/或酚基。 作为引入这些基团的方法,可以以最推荐的方式使用相应的共聚物的形成。 作为示例,膜可以包含具有环状结构单元和侧链型磺酸基团的氟化聚合物。
    • 99. 发明授权
    • Cellular metal by electrolysis
    • 电解质细胞金属
    • US4053371A
    • 1977-10-11
    • US691692
    • 1976-06-01
    • Frank E. Towsley
    • Frank E. Towsley
    • C25B1/46C25B11/03C25D1/08C25D5/54C25D7/04
    • C25B1/46C25B11/03C25D1/08
    • A cellular metal structure comprising a continuous interconnected network of electrolytically deposited metal defining a plurality of substantially convex cellular compartments therebetween is disclosed. The metal structure is produced by positioning a cellular array of substantially convex and substantially electrically nonconductive particles having a plurality of interstitial spaces therebetween between the anode and cathode of an electrolytic cell. The array is at least partially immersed in an aqueous solution of an electrolyte suitable for the electrolytic deposition of the metal. A direct current potential is applied between the anode and cathode to electrolytically deposit a continuous interconnected network of metal in the interstitial spaces defined between the cellular array of substantially convex particles.
    • 本发明涉及具有位于阳极室内的阳极和位于适于容纳阴极电解液的阴极室内的氧化性气体去极化阴极的电解池的改进,所述阴极室通过阳离子可透过隔板与阳极室间隔开 。 改进的电池包括具有多孔金属结构的阴极,该多孔金属结构包括电解沉积金属的连续互连网络,其间限定多个基本上凸起的和基本上不导电的细胞隔室。 隔室的布置适于允许氧化气体通过阴极电解液。 多孔金属结构的特征还在于沉积的金属与多孔金属结构内的细胞隔室接触。