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    • 11. 发明授权
    • Activated electrodes
    • 活性电极
    • US4584065A
    • 1986-04-22
    • US644829
    • 1984-08-27
    • Jiri DivisekHeinz SchmitzHeinz Wullenweber
    • Jiri DivisekHeinz SchmitzHeinz Wullenweber
    • C25B11/04C25B11/00C25B11/06C25D1/08C25D1/20C25D5/48
    • C25B11/00
    • A process for the manufacture of thin activated electrodes including a base metal, which can be iron, cobalt or nickel, with a good adhering active surface layer. Both the base metal and the surface layer are galvanically sequentially deposited as separate layers on a removable electrically-conductive carrier. The surface layer is deposited as an activatable alloy including the base metal and a leachable metal, particularly zinc. The galvanizing deposited layers are subsequently separated as a unit from the carrier. The alloy is activated by leaching the leachable metal therefrom before, during or after separation of the carrier. Two activatable layers of alloy can be deposited on the carrier with a layer of the base metal deposited between the alloy layers.
    • 用于制造薄的活化电极的方法,其包括可以是铁,钴或镍的贱金属,具有良好的附着活性表面层。 基底金属和表面层均以电流顺序地沉积在可移除的导电载体上作为单独的层。 表面层作为可活化的合金沉积,包括贱金属和可浸出的金属,特别是锌。 随后将镀锌沉积层作为单元与载体分离。 通过在载体分离之前,期间或之后从其中浸出可浸出的金属来活化合金。 两个可活化的合金层可以沉积在载体上,一层沉积在合金层之间的基体金属。
    • 14. 发明授权
    • Electrochemical gas analyzer for determination of sulphur dioxide
content of gases
    • 用于测定气体二氧化硫含量的电化学气体分析仪
    • US4532023A
    • 1985-07-30
    • US585431
    • 1984-03-02
    • Leander FurstJiri Divisek
    • Leander FurstJiri Divisek
    • G01N27/49G01N27/50
    • G01N27/4045
    • The invention is concerned with an electrochemical gas analyzer for determining the sulphur dioxide content of certain gases in particular, flue gases. The device comprises a measuring cell containing a measuring electrode for the determination of the depolarization current and further comprising an unpolarizable electrode in the same electrolyte. The gas input flow is utilized to cause a circulation of electrolyte containing the dissolved gas which moves in the space between the measuring and counter-electrode. The electrolyte is continuously renewed and the electrolyte leaving the cell is regeneratd and recycled. The sulphur dioxide dissolved in the electrolyte is removed outside the cell by treatment with air in the presence of activated charcoal.
    • 本发明涉及用于确定某些气体,特别是烟道气体的二氧化硫含量的电化学气体分析仪。 该装置包括含有用于确定去极化电流的测量电极的测量单元,并且在同一电解质中还包括不可极化的电极。 气体输入流被用于引起电解质的循环,所述电解质含有在测量和对电极之间的空间中移动的溶解的气体。 电解液不断更新,离开电池的电解质被再生并循环使用。 溶解在电解质中的二氧化硫在活性炭存在下通过用空气处理除去在电池外面。
    • 16. 发明授权
    • Diaphragms for alkaline water electrolysis and method for production of
the same as well as utilization thereof
    • 碱性水电解用隔膜及其制造方法及其利用
    • US4394244A
    • 1983-07-19
    • US166448
    • 1980-07-07
    • Jiri DivisekJurgen Mergel
    • Jiri DivisekJurgen Mergel
    • C25B1/04C25B13/02C25B13/04
    • C25B13/04C25B1/04Y02E60/366
    • A diaphragm of porous sinter material for alkaline water electrolysis characterized by a porous sinter metal oxidized at least partially to metal oxide. A frame structure of the sinter body is provided especially wire net. The base metal of the sinter body is formed by nickel, iron or copper. The method includes forming a porous metal sinter body and oxidizing the same at elevated temperature in oxygen-containing atmosphere. The method for production of nickel oxide diaphragms furthermore includes applying to a nickel net a pasty mass of nickel powder containing a binder and burning. Applying in a thin layer as by brushing nickel powder of a particle size of about 1 to 10 mm in a rubber solution in toluene upon a carrier, especially a nickel net, and this arrangement is subjected to sintering at 700.degree. to 1,000.degree. C. for a time or duration of 10 to 20 minutes in inert or reducing atmosphere especially in hydrogen and the sinter body which is obtained is subjected to roasting in air at 1000.degree. C. to 1200.degree. C. up to three hours, especially for a time duration in a range of between ten and forty minutes. The diaphragms are produced with a thickness in a range of approximately 1 mm, especially in a range of approximately 0.3 mm to 0.7 mm. Utilization of the diaphragm includes electrolysis cells with active porous nickel electrode fixed on the diaphragm in a sandwich manner of construction.
    • 用于碱性水电解的多孔烧结材料的隔膜,其特征在于至少部分氧化成金属氧化物的多孔烧结金属。 烧结体的框架结构尤其是线网。 烧结体的基体金属由镍,铁或铜形成。 该方法包括在含氧气氛中形成多孔金属烧结体并在升高的温度下对其进行氧化。 制造氧化镍隔膜的方法还包括向镍网施加含有粘合剂和燃烧的糊状的镍粉末。 通过在载体,特别是镍网上的甲苯中的橡胶溶液中将约1〜10毫米粒度的镍粉刷涂在薄层中,并将该配置在700℃至1000℃下进行烧结。 在惰性或还原气氛(特别是氢气)中持续10至20分钟的时间或持续时间,将获得的烧结体在空气中在1000℃至1200℃下焙烧至三小时,特别是一段时间 持续时间在十到四十分钟之间。 膜片的厚度在大约1mm的范围内,特别是在大约0.3mm至0.7mm的范围内。 隔膜的利用包括以活动的多孔镍电极的电解电池,其以三明治结构的方式固定在隔膜上。