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    • 2. 发明申请
    • Cathode for a direct methanol fuel cell and method for operating the same
    • 直接甲醇燃料电池的阴极及其操作方法
    • US20070128502A1
    • 2007-06-07
    • US10553574
    • 2004-04-08
    • Hendrik DohleMartin MullerJan BringmannJurgen MergelDetlef Stolten
    • Hendrik DohleMartin MullerJan BringmannJurgen MergelDetlef Stolten
    • H01M4/94H01M8/10
    • H01M4/8605H01M8/04156H01M8/1004H01M8/1009H01M2004/8689Y02E60/523
    • In low-temperature fuel cells according to prior art, the problem often arises that the diffusion layer of the cathode is filled by water which is permeated or produced on the cathode, such that oxygen can no longer be transported to the catalyst layer of the cathode in a frictionless manner. As a result, said fuel cells are regularly used with a high excess of oxygen in order to reduce the cited transport problems for the oxygen. The inventive fuel cell enables said problem to be solved in that the arrangement of the diffusion layer and the catalyst layer of the cathode is inverted. The diffusion layer, which is embodied in such a way as to also conduct ions, is directly adjacent to the electrolyte membrane. The catalyst layer oriented towards the free cathode space can advantageously directly react with the supplied oxygen without further transport problems. A further advantage lies in the fact that the water produced on the catalyst layer of the cathode and/or permeated by the electrolyte membrane and the diffusion layer can be easily withdrawn via the free cathode space.
    • 在根据现有技术的低温燃料电池中,经常出现的问题是阴极的扩散层被在阴极上渗透或产生的水填充,使得氧不再能够传输到阴极的催化剂层 以无摩擦的方式。 结果,所述燃料电池常规地使用大量的氧气,以便减少所引用的氧气运输问题。 本发明的燃料电池能够解决这个问题,即扩散层和阴极的催化剂层的布置被反转。 以能够进行离子的方式实施的扩散层与电解质膜直接相邻。 朝向自由阴极空间取向的催化剂层可以有利地直接与供应的氧气反应,而不会有进一步的运输问题。 另一个优点在于,可以通过自由阴极空间容易地排出在阴极的催化剂层上产生的和/或被电解质膜和扩散层渗透的水。
    • 3. 发明申请
    • Device for cleaning waste gases for a direct alcohol fuel cell or for a fuel cell stack constructed therefrom
    • 用于清洁用于直接醇燃料电池或由其构成的燃料电池堆的废气的装置
    • US20050084729A1
    • 2005-04-21
    • US10496069
    • 2002-11-12
    • Hendrik DohleJurgen Mergel
    • Hendrik DohleJurgen Mergel
    • B01D53/86H01M2/00H01M8/04186H01M8/0662H01M8/1009H01M8/2455H01M8/04
    • B01D53/8668H01M8/04186H01M8/0662H01M8/1009H01M8/2455Y02E60/522
    • The invention relates to a device for cleaning waste gases for a direct alcohol fuel cell or for a direct alcohol fuel cell stack, comprising at least one supply line for supplying an oxidizing agent into a cathode space of a fuel cell and at least one evacuation line for evacuating waste gas out of a fuel cell. The supply line and evacuation line are arranged next to one another at least in one area and are separated by a porous layer. A catalytic converter is placed on the surface of the porous layer oriented toward the evacuation line. In the inventive waste gas cleaning device, the advantages of an internal utilization of heat and of an at least partial water circuit with an effective catalytic conversion and reduction of removed non-converted alcohol, particularly methanol, locally unite at one location of the fuel cell system. The waste gas cleaning device simultaneously serves to preheat and wet the supplied oxidizing agent and can be advantageously provided with a very compact design.
    • 本发明涉及一种用于清洁直接醇燃料电池或直接醇燃料电池堆的废气的装置,包括用于将氧化剂供应到燃料电池的阴极空间中的至少一条供应管线和至少一个排气管线 用于将废气排出燃料电池。 供应管线和排气管线至少在一个区域中彼此相邻布置,并被多孔层分隔开。 将催化转化器放置在朝向排气管线的多孔层的表面上。 在本发明的废气清洁装置中,内部利用热量和至少部分水回路的优点是有效催化转化和还原除去的未转化的醇,特别是甲醇,在燃料电池的一个位置局部地团聚 系统。 废气清洁装置同时用于预热和湿润供应的氧化剂,并且可以有利地提供非常紧凑的设计。
    • 5. 发明授权
    • Hybrid process for producing hydrogen
    • 用于生产氢的混合工艺
    • US4256549A
    • 1981-03-17
    • US119107
    • 1980-02-06
    • Jiri DivisekJurgen Mergel
    • Jiri DivisekJurgen Mergel
    • C25B1/04C25B1/02
    • C25B1/02Y02E60/366
    • A method for producing hydrogen according to a hybrid process. A low oxide,hich is formed at a high temperature from a higher oxide accompanied by splitting-off of oxygen, is introduced into an aqueous electrolyte and is reoxidized anodically along with simulataneous cathodic hydrogen generation. The oxide is returned into the high temperature range. As an oxide, antimony oxide, especially antimony tetraoxide, is used, with the oxide being formed anodically in a melt-flow electrolysis and being decomposed again into antimony trioxide and oxygen at approximately 850.degree. to 1000.degree. C. As an electrolyte, an alkali melt, and especially a melt having a sodium hydroxide base, may be used. The electrolyte may be formed by a possibly salt, especially sodium fluoride, containing mixture of sodium hydroxide and antimony trioxide in a mole ratio of 1:0.5 to 1:5.0, with a water content of approxaimately 1 to 5% by weight. The anode chamber is separated from the cathode chamber by a .beta.-aluminum oxide separating wall.
    • 根据混合方法生产氢的方法。 在高温下形成的低氧化物,伴随着氧的分离,被引入到水性电解质中,并且随着阴极生成氢气而被阳极氧化再氧化。 氧化物回到高温范围。 作为氧化物,使用氧化锑,特别是四氧化锑,其中氧化物在熔体流动电解中阳极形成,并在约850℃至1000℃下再次分解成三氧化锑和氧。作为电解质, 熔融,特别是具有氢氧化钠基的熔体。 电解质可以由可能的盐,特别是氟化钠,含有摩尔比为1:0.5至1:5.0的氢氧化钠和三氧化锑的混合物形成,水含量为约1-5重量%。 阳极室通过β-氧化铝分隔壁与阴极室分离。
    • 8. 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。