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    • 3. 发明授权
    • Process for the catalytic reduction of reducible compounds in solution
    • 在溶液中催化还原可还原化合物的方法
    • US4159309A
    • 1979-06-26
    • US889727
    • 1978-03-24
    • Wolfgang FaulBertel Kastening
    • Wolfgang FaulBertel Kastening
    • C02F1/70C02F1/76C02F9/00C01B21/00C01C1/00
    • C02F1/70C02F2101/16C02F2101/22C02F2303/185
    • Reducible pollutants can be detoxified by reduction and metals can be recred by reduction of the corresponding metal ions by bringing into contact a catalyst with the solution which is suitable for the electrochemical reduction of the ions in question, and mixing into the solution (or bubbling therethrough in the case of a gas) a reducing agent that has a redox potential in the redox system of the reducing agent and its oxidation product that is more negative than the redox potential of the substance to be reduced and its reduction product. The catalyst is a material that is suitable for use as an anode material at which hydrogen can be oxidized in a fuel cell. Such catalysts include finely divided platinum, activated carbon coated with platinum, tungsten carbide and activated carbon coated with tungsten carbide, particularly. Hydrogen is a good reducing agent for the purpose.
    • 可降解的污染物可以通过还原进行解毒,并且可以通过使催化剂与适合所述离子的电化学还原的溶液接触催化剂并将其混合到溶液中 在气体的情况下)还原剂在还原剂的氧化还原体系中具有氧化还原电位,其氧化产物比待还原物质的氧化还原电位更负,其还原产物。 催化剂是适合用作在燃料电池中氢被氧化的阳极材料的材料。 这种催化剂包括细碎的铂,涂覆有铂的活性炭,碳化钨和涂有碳化钨的活性炭。 氢是一种很好的还原剂。
    • 5. 发明授权
    • Apparatus for electrochemically processing metallic surfaces
    • 用于电化学处理金属表面的装置
    • US4153531A
    • 1979-05-08
    • US881638
    • 1978-02-27
    • Wolfgang FaulBertel Kastening
    • Wolfgang FaulBertel Kastening
    • C25F3/02C25F7/00H05K3/07C25D17/06
    • H05K3/07C25F3/02C25F7/00H05K2203/09
    • An electrolytic cell which between the anode and cathode includes a diaphm dividing the electrolytic cell into two chambers. In one of these chambers there is provided an electrolyte which contains the suspension of electrically conductive bodies. The apparatus includes a treatment chamber for workpieces to be arranged in a contact-free manner with regard to the cathode and anode. A conveying line for the electrolyte containing the electrically conductive bodies extends between on one hand that chamber of the electrolytic cell in which the electrode charging the electrically conductive bodies is arranged, and on the other hand the treatment chamber. One portion of said conveying line outside the electrolytic cell includes a porous wall which is permeable for the electrolyte but retains electrically conductive bodies. The annular chamber formed by a surrounding outer pipe and porous wall which surrounds the conveying line communicates with the chamber containing the counter-electrode in the electrolytic cell for exchanging electrolyte.
    • 在阳极和阴极之间的电解池包括将电解槽分成两个室的隔膜。 在这些腔室之一中,提供了包含导电体的悬浮液的电解质。 该装置包括用于工件的处理室,其相对于阴极和阳极以无接触的方式布置。 用于含有导电体的电解质的输送管线一方面延伸在其中布置有导电体的电极的电解槽的腔室,另一方面是处理室。 所述输送线在电解池外部的一部分包括多孔壁,该多孔壁对于电解质是可渗透的,但保留导电体。 由围绕输送线的周围的外管和多孔壁形成的环形室与电解槽中包含反电极的室连通,用于交换电解质。
    • 6. 发明授权
    • Method and apparatus for regenerating an ammoniacal etching solution
    • 用于再生氨蚀刻溶液的方法和装置
    • US4576677A
    • 1986-03-18
    • US598087
    • 1984-04-09
    • Wolfgang FaulLeander FurstWalter HolzerBertel Kastening
    • Wolfgang FaulLeander FurstWalter HolzerBertel Kastening
    • C23F1/46C23F1/00B44C1/22C03C15/00C03C25/06
    • C23F1/46
    • Ammoniacal etching solution containing metal ions as the result of etching is withdrawn from an etching bath and while part of it goes to an electrolysis cell for removal of metal ion, the remainder goes back to the etching bath through a liquid jet pump in which it serves as the working liquid, while the pump sucks in from the electrolysis cell the anodically evolved oxygen. The thorough mixing of the oxygen into the etching solution performed by the pump results in oxidation so rapid that in many cases it becomes unnecessary to suspend catalyst particles in the electrolyte to accelerate the oxidative regeneration of the etching solution. Where use of such particles is still desired, the solution drawn from the etching bath goes through a cylindrical filter unit from which a filtrate is drawn off laterally for the electrolysis cell, while the remainder of the input goes to the jet pump. Controls are provided for using the electrolysis cell only when the metal ion concentration is above a predetermined value, for adding ammonia to the oxygen line in order to maintain a particular value of pH and for controlling the temperature of the electrolyte in the electrolysis cell in order that a desired quantity of water can be condensed from the oxygen line for use in rinsing the work pieces after they are taken out of the etching bath.
    • 作为蚀刻结果含有金属离子的氨蚀刻溶液从蚀刻浴中取出,并且其一部分进入用于去除金属离子的电解槽,其余部分通过液体喷射泵返回到蚀刻槽 作为工作液体,当泵从电解槽吸入阳极放出的氧气。 将氧气彻底混合到由泵执行的蚀刻溶液中导致氧化如此快速,使得在许多情况下不需要将催化剂颗粒悬浮在电解质中以加速蚀刻溶液的氧化再生。 在仍然需要使用这种颗粒的情况下,从蚀刻浴中抽出的溶液通过圆柱形过滤器单元,其中滤液被横向排出用于电解池,而剩余的输入进入喷射泵。 提供了仅当金属离子浓度高于预定值时才使用电解池的控制,以便为了保持特定的pH值和为了控制电解槽中的电解质的温度按顺序向氧线添加氨 可以从工作片从蚀刻槽中取出所需量的水从氧气线上冷凝,以用于冲洗工件。
    • 9. 发明授权
    • Method of regenerating an ammoniacal etching solution
    • 再生氨蚀刻液的方法
    • US4385969A
    • 1983-05-31
    • US287492
    • 1981-07-27
    • Bertel KasteningWolfgang FaulLeander FurstWalter Holzer
    • Bertel KasteningWolfgang FaulLeander FurstWalter Holzer
    • C23F1/40C23F1/46H05K3/06C25C1/12C25C1/00C25C1/16
    • C23F1/46
    • In addition to catalyzing the reoxidization of spent alkaline etching age the suspension of activated carbon powder in the etching solution also increases the speed of etching when the etching solution is recirculated in the etching of printed circuit boards. The ammonium sulfate etching solution is set to a pH of about 9 by the addition of ammonia gas. In the recirculation of the etching solution, a part of the solution can be freed by filtration from suspended carbon particles and passed through the cathode and anode chambers of an electrolysis cell for the recovery of the etched metal by deposition on the cathode. The activated carbon powder for this purpose is calcined before use, at a temperature of between 900.degree. and 1200.degree. C. in vacuum or in an atmosphere that is inert, reducing, or only slightly oxidizing as in the case of an atmosphere containing carbon dioxide, water vapor or both, in a concentration that does not appreciably oxidize the carbon particles.
    • 除了催化废碱蚀刻剂的再氧化之外,当在印刷电路板的蚀刻中蚀刻溶液再循环时,活性炭粉末在蚀刻溶液中的悬浮液也增加了蚀刻速度。 通过加入氨气使硫酸铵蚀刻溶液的pH设定为约9。 在蚀刻溶液的再循环中,溶液的一部分可以通过从悬浮碳颗粒过滤而被除去,并通过电解槽的阴极和阳极室,以通过沉积在阴极上来回收蚀刻的金属。 用于此目的的活性炭粉末在使用前煅烧,在真空中或在惰性,还原或仅微量氧化的气氛中在900℃至1200℃的温度下,如在含有二氧化碳的气氛中 ,水蒸气或两者,浓度不会明显地氧化碳颗粒。