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    • 1. 发明授权
    • Electrolysis cell and method for electrolytic production of hydrogen
    • 电解槽和氢电解生产方法
    • US4330378A
    • 1982-05-18
    • US208933
    • 1980-11-21
    • Dagmar BoltersdorfRobert JungingerBernd D. StruckHerbert Neumeister
    • Dagmar BoltersdorfRobert JungingerBernd D. StruckHerbert Neumeister
    • C25B1/02C25B1/22C25B9/00C25B9/08
    • C25B9/08C25B1/02C25B1/22
    • The production of hydrogen by electrolysis in a cell, in which the anode electrolyte contains sulfur dioxide as well as sulfuric acid and an intermediate chamber separated from the anode and cathode chambers by cation-exchanger membranes is provided through which an electrolyte flows in order to prevent sulfur dioxide from reaching the cathode chamber is greatly improved by using as the anode side membrane a cation-exchanger in which a polyvinyl chloride skeleton is combined with a polymer of styrol and divinyl benzol to which sulfonic acid groups have been attached, such a membrane having a very low resistivity, thus reducing the necessary electrolysis voltage. Such a membrane also loses conductivity with increasing sulfuric acid concentration at a lower rate than membranes previously used in such an electrolysis process and permits a higher sulfuric acid concentration in the anode electrolyte. The improvement on the anode side makes possible the operation of the cathode at low sulfuric acid electrolyte concentration, below 20 or even 10% by weight. Through-flow electrodes of porous graphite encased except on the membrane side by impermeable graphite further improve the operation of the process, especially if they fill the electrolyte chamber right up to the membrane.
    • 通过在电池中电解生产氢,其中阳极电解质含有二氧化硫以及硫酸,以及通过阳离子交换膜从阳极室和阴极室分离的中间室,通过电解液流过以防止 通过将聚氯乙烯骨架与其中已经连接有磺酸基团的苯乙烯和二乙烯基苯酚的聚合物组合的阳离子交换剂用作阳极侧膜,可以大大改善到达阴极室的二氧化硫,这样的膜具有 电阻率非常低,从而减少必要的电解电压。 这样的膜也会随着硫酸浓度的增加而以比先前在这种电解方法中使用的膜低的速率降低导电性并允许阳极电解质中的较高的硫酸浓度。 在阳极侧的改进使阴极在低硫酸电解质浓度下的操作成为可能,低于20甚至10重量%。 通过不渗透石墨在膜侧除外的多孔石墨的通流电极进一步改善了该方法的操作,特别是如果它们将电解液室填充到膜上。
    • 2. 发明授权
    • Method for electrolytic production of hydrogen
    • 电解生产氢的方法
    • US4391682A
    • 1983-07-05
    • US228796
    • 1981-01-26
    • Bernd D. StruckRobert JungingerDagmar Boltersdorf
    • Bernd D. StruckRobert JungingerDagmar Boltersdorf
    • C25B1/02C25B1/22
    • C25B1/22C25B1/02
    • A reduction of the voltage across the electrolysis cell in which hydrogen is produced in the sulfuric acid hybrid closed cycle process by use of an electrolysis cell having an intermediate chamber between the anode and cathode chamber through which a separate electrolyte is caused to flow, is obtainable under operation with the electrolytes in both the cathode and the anode chambers having a concentration of sulfuric acid by weight of about 50% or more. It is found that the undesired formation of hydrogen sulfide and of sulfur remains at a tolerable small level if the catholyte is continuously renewed. A low specific resistance cation membrane is preferably used between the cathode and intermediate chambers, as well as between the anode and intermediate chambers.
    • 可以通过使用在阳极室和阴极室之间具有中间室的电解池在硫酸混合封闭循环过程中产生氢的电解池中的电压降低,通过该中间室使单独的电解液流过。 在阴极和阳极室中的电解质的操作中,其浓度为约50重量%以上的硫酸浓度。 发现如果阴极电解液连续更新,硫化氢和硫的不期望的形成将保持在可容许的小水平。 优选在阴极和中间室之间以及阳极和中间室之间使用低电阻率阳离子膜。
    • 5. 发明授权
    • Method of recovering hydrogen and oxygen from water
    • 从水中回收氢和氧的方法
    • US4164457A
    • 1979-08-14
    • US917842
    • 1978-06-22
    • Heiko BarnertMieczyslaw PerecBernd D. Struck
    • Heiko BarnertMieczyslaw PerecBernd D. Struck
    • C25B1/04C01B3/02C01B13/02C25B1/02C25B1/22C01B13/00
    • C25B1/02C25B1/22Y02E60/366
    • A method of recovering hydrogen and oxygen from water. Water and sulfur dide are supplied to, and hydrogen and sulfuric acid are removed from, a galvanic or electrolytic cell. Hydrogen ions are electrochemically liberated by anodic oxidation of the supplied sulfur dioxide accompanied by decomposition of the water and formation of sulfuric acid in the anolyte, and hydrogen gas is electrolytically generated at the cathode from the hydrogen ions. To evaporate water, electrolytic solution is removed from the anode chamber of the galvanic cell. The anode chamber is separated from the cathode chamber by means of a membrane. After the ensuing evaporation, the thus formed anhydride of the sulfuric acid is decomposed by being heated, and is accompanied by the formation of oxygen and sulfur dioxide gas. The sulfur dioxide is oxidized at a carbon and/or graphite anode in the presence of very small quantities, e.g. a minimum of 0.005% by weight, of hydriodic acid in the anolyte. The hydriodic acid which is found in that portion of the electrolyte which is removed from the anode chamber is evaporated together with the water. The evaporated water, together with the evaporated hydriodic acid, are again supplied to the anode chamber.
    • 从水中回收氢和氧的方法。 供应水和二氧化硫,从电镀或电解池中除去氢和硫酸。 通过所供应的二氧化硫的阳极氧化伴随着水的分解和在阳极电解液中形成硫酸而电化学释放氢离子,并且氢气在阴极从氢离子电解产生。 为了蒸发水,从电池的阳极室去除电解液。 阳极室通过膜与阴极室分离。 在随后的蒸发之后,由此形成的硫酸酐被加热分解,伴随着形成氧气和二氧化硫气体。 二氧化硫在非常少量的存在下在碳和/或石墨阳极氧化,例如, 至少0.005重量%的阳离子中的氢碘酸。 在从阳极室除去的电解质部分中发现的氢碘酸与水一起蒸发。 蒸发的水与蒸发的氢碘酸一起再次供应到阳极室。
    • 6. 发明授权
    • Electrolysis cell with intermediate chamber for electrolyte flow
    • 具有电解液流中间室的电解槽
    • US4443316A
    • 1984-04-17
    • US318457
    • 1981-11-05
    • Bernd D. Struck
    • Bernd D. Struck
    • C25B9/08C25B13/00C25B9/00C25B13/02C25B13/08
    • C25B9/08C25B13/00
    • The economy of production of hydrogen and sulfuric acid in a three chamberlectrolysis cell in which an electrolyte flows through the intermediate chamber (11) which is bounded by ion exchanger membranes (9,10) can be improved by the provision of a porus supporting framework or skeleton (12) of graphite or of ion exchanger material against which the separators with the electrodes (7, 8) on them, can be pressed. The overall internal resistance of the cell can thus be reduced and its mechanical behavior improved. Substantial through passage porosity is desired in the supporting structure, which may be of graphite, but porous aggregates of ion exchanger material with fixedly applied or welded on separators in the form of stacked layers or rolled mats, are preferred for the relative simplicity of their provision in practice.
    • 电解质流过通过离子交换膜(9,10)界定的中间室(11)的三室电解池中的氢和硫酸的生产经济可以通过提供孔结构框架 或石墨或离子交换器材料的骨架(12),其上具有电极(7,8)的分离器可以被按压。 因此,可以减小电池的整体内阻,并改善其机械性能。 对于可能是石墨的支撑结构,需要通过通道孔隙的重要性,但是优选的是它们提供的相对简单的方式,其中离子交换材料的多孔聚集体固定地施加或焊接在叠层或轧制垫的形式的隔板上 在实践中。
    • 9. 发明授权
    • Process for the electrolysis of sulfur dioxide solutions
    • 二氧化硫溶液电解工艺
    • US4304643A
    • 1981-12-08
    • US66861
    • 1979-08-15
    • Jiri DivisekHeinrich SchmitzBernd D. Struck
    • Jiri DivisekHeinrich SchmitzBernd D. Struck
    • C25B1/02C25B1/22C25B1/00
    • C25B1/22C25B1/02
    • Particles of electrically conducting activated carbon of about 500 to 1,000 m.sup.2 /g specific surface added to an electrolyte provided by a solution of sulfur dioxide in water are found to provide a substantial reduction of the electrical energy requirement in the electrolysis of such an electrolyte for the production of hydrogen and sulfuric acid. A further reduction of energy consumption is obtained by additionally introducing iodine in the electrolyte in an amount not exceeding 1% by weight of the entire solution. Use of an anode in which the surface of a graphite base body is coated with a thin layer of activated carbon bonded to the graphite body by means of a binder, such as rubber, also reduces the electrical energy requirement for the electrolysis. To coat the surface of the electrode, carbon particles are first dispersed in a rubber solution and the suspension is then applied to the surface of the graphite body as a thin layer.
    • 发现添加到由二氧化硫溶于水的电解质中提供的电解质的约500至1,000m 2 / g比表面积的导电活性炭颗粒可显着减少用于电解的电解质中的电能需求 生产氢和硫酸。 通过在电解液中另外引入碘量不超过整个溶液的1重量%,可以进一步降低能量消耗。 使用阳极,其中石墨基体的表面涂覆有通过诸如橡胶的粘合剂结合到石墨体的活性炭的薄层,还降低了电解所需的电能。 为了涂覆电极的表面,首先将碳颗粒分散在橡胶溶液中,然后将悬浮液作为薄层施加到石墨体的表面。