Electrode and electrochemical cell
    2.
    发明授权
    Electrode and electrochemical cell 失效
    电极和电化学电池

    公开(公告)号:US5972181A

    公开(公告)日:1999-10-26

    申请号:US106411

    申请日:1998-06-29

    摘要: An electrode, electrochemical cell, and electrochemical processes are disclosed. The electrode is a porous, multi-layered electrode which can have an element in flexible, strip form wound around a central, usually flat plate core, which core may serve as a current distributor. In any form, each layer can be represented by a very thin, highly flexible metal mesh. This can be a fine, as opposed to a coarse, mesh which has extremely thin strands and small voids. The electrode will have an active coating. For utilizing this electrode, the cell in one form will be a monopolar cell providing upward, parallel electrolyte flow through the porous, multi-layered electrode. A representative cell can have such electrode at least substantially filling an electrode chamber. The cells can be contained in a cell box that will provide the desired flow-through relationship for the electrolyte to the electrode. In cell operation, electrochemical processes which can be carried out include metal ion oxidation or reduction, oxidation of organic substituents, nitrate reduction as well as salt splitting.

    摘要翻译: 公开了一种电极,电化学电池和电化学方法。 电极是多孔的多层电极,其可以具有缠绕在中心的,通常为平的板芯上的柔性带状的元件,该芯可以用作电流分布器。 以任何形式,每层可以由非常薄的,高度柔性的金属网表示。 这可以是细的,而不是具有极细线和小空隙的粗网。 电极将具有活性涂层。 为了利用该电极,一种形式的电池将是单极电池,其提供通过多孔多层电极的向上平行的电解质流。 代表性的电池可以具有至少基本上填充电极室的这种电极。 细胞可以包含在细胞盒中,其将为电解质提供期望的流通关系。 在电池操作中,可以进行的电化学过程包括金属离子氧化还原,有机取代基的氧化,硝酸盐的还原以及盐分解。

    Cell having electrodes of improved service life
    6.
    发明授权
    Cell having electrodes of improved service life 失效
    电池具有使用寿命更长的电极

    公开(公告)号:US5435896A

    公开(公告)日:1995-07-25

    申请号:US217830

    申请日:1994-03-25

    摘要: A metal surface, useful as an electrode in an electrolytic cell, is now described having enhanced adhesion of subsequently applied coatings combined with excellent coating service life. The substrate metal of the electrode, such as a valve metal as represented by titanium, is provided with a highly desirable rough surface characteristic for subsequent coating application. This can be achieved by various operations including etching and melt spray application of metal or ceramic oxide to ensure a roughened surface morphology. Usually in subsequent operations, a barrier layer is provided on the surface of enhanced morphology. This may be achieved by operations including heating, as well as including thermal decomposition of a layer precursor. Subsequent coatings provide enhanced lifetime even in the most rugged commercial environments.

    摘要翻译: 现在描述用作电解池中的电极的金属表面,其具有增强的随后涂覆的涂层的粘附性以及优异的涂层使用寿命。 电极的基板金属,例如由钛表示的阀金属,具有用于后续涂布应用的高度期望的粗糙表面特性。 这可以通过各种操作实现,包括蚀刻和熔体喷涂金属或陶瓷氧化物以确保粗糙化的表面形态。 通常在随后的操作中,在增强的形态表面上提供阻挡层。 这可以通过包括加热以及包括层前体的热分解的操作来实现。 随后的涂层即使在最坚固的商业环境中也能提供更长的使用寿命。

    Diaphragm cell
    7.
    发明授权
    Diaphragm cell 有权
    隔膜池

    公开(公告)号:US06395153B1

    公开(公告)日:2002-05-28

    申请号:US09655967

    申请日:1999-09-10

    IPC分类号: C25B900

    CPC分类号: C25B9/08 C25B1/46 C25B15/00

    摘要: The present invention pertains to electrolytic diaphragm cells, particularly for the electrolysis of brine to produce chlorine and caustic. The innovation resides generally in the discovery that electrolytic cell operation can be desirably enhanced by compressing the diaphragm between anode and cathode. This compression of the diaphragm reduces the diaphragm thickness from an original thickness, e.g., from an original thickness of a diaphragm freshly deposited on a cathode. The reduced thickness of the diaphragm provides for cell operation that is less than zero gap operation. By maintaining the diaphragm under compression and in a reduced thickness, the cell operates with a narrower interelectrode gap and consequently at a desirably reduced cell voltage.

    摘要翻译: 本发明涉及电解隔膜电池,特别是用于电解盐水以产生氯和苛性碱。 该创新通常在于通过在阳极和阴极之间压缩膜片可以期望提高电解池操作的发现。 隔膜的这种压缩使隔膜厚度从原始厚度减小,例如从刚刚沉积在阴极上的隔膜的原始厚度。 膜片的减小的厚度提供小于零间隙操作的电池操作。 通过将隔膜保持在压缩和减小的厚度下,电池以更窄的电极间间隙运行,并因此以期望的电池电压降低。

    Electrochemical process
    8.
    发明授权
    Electrochemical process 失效
    电化学工艺

    公开(公告)号:US5705051A

    公开(公告)日:1998-01-06

    申请号:US632574

    申请日:1996-04-15

    摘要: An electrode, electrochemical cell, and electrochemical processes are disclosed. The electrode is a porous, multi-layered electrode which can have an element in flexible, strip form wound around a central, usually flat plate core, which core may serve as a current distributor. In any form, each layer can be represented by a very thin, highly flexible metal mesh. This can be a fine, as opposed to a coarse, mesh which has extremely thin strands and small voids. The electrode will have an active coating. For utilizing this electrode, the cell in one form will be a monopolar cell providing upward, parallel electrolyte flow through the porous, multi-layered electrode. A representative cell can have such electrode at least substantially filling an electrode chamber. The cells can be contained in a cell box that will provide the desired flow-through relationship for the electrolyte to the electrode. In cell operation, electrochemical processes which can be carried out include metal ion oxidation or reduction, oxidation of organic substituents, nitrate reduction as well as salt splitting.

    摘要翻译: 公开了一种电极,电化学电池和电化学方法。 电极是多孔的多层电极,其可以具有缠绕在中心的,通常为平的板芯上的柔性带状的元件,该芯可以用作电流分布器。 以任何形式,每层可以由非常薄的,高度柔性的金属网表示。 这可以是细的,而不是具有极细线和小空隙的粗网。 电极将具有活性涂层。 为了利用该电极,一种形式的电池将是单极电池,其提供通过多孔多层电极的向上平行的电解质流。 代表性的电池可以具有至少基本上填充电极室的这种电极。 细胞可以包含在细胞盒中,其将为电解质提供期望的流通关系。 在电池操作中,可以进行的电化学过程包括金属离子氧化还原,有机取代基的氧化,硝酸盐的还原以及盐分解。

    Electrocatalytic electrode
    10.
    发明授权
    Electrocatalytic electrode 失效
    电催化电极

    公开(公告)号:US4517068A

    公开(公告)日:1985-05-14

    申请号:US527552

    申请日:1983-08-26

    CPC分类号: C25B11/0484

    摘要: An electrode, especially for chlorine and hypochlorite production, comprises an electrocatalyst consisting of 22-55 mol % ruthenium oxide, 0.2-22 mol % palladium oxide and 44-77.8 mol % titanium oxide. The electrocatalyst may form a coating on a valve metal substrate and may be topcoated with a porous layer of titanium or tantalum oxide.

    摘要翻译: PCT No.PCT / US81 / 01763 Sec。 371日期:1983年8月26日 102(e)日期1983年8月26日PCT提交1981年12月28日PCT公布。 公开号WO83 / 02288 日期:1983年7月7日。一种特别用于氯和次氯酸盐生产的电极包括由22-55mol%氧化钌,0.2-22mol%氧化钯和44-77.8mol%二氧化钛组成的电催化剂。 电催化剂可以在阀金属基材上形成涂层,并且可以用多孔层的钛或氧化钽涂覆。