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    • 3. 发明专利
    • TREATMENT OF ION EXCHANGE RESIN OF ELECTROLYTIC CELL
    • JP2000117060A
    • 2000-04-25
    • JP30476898
    • 1998-10-12
    • CHLORINE ENG CORP LTD
    • MARUMOTO MASATAKAARIMOTO OSAMUKISHI TAKEMICHI
    • B01D61/52C02F1/469C25B9/00C25B9/08C25B13/08
    • PROBLEM TO BE SOLVED: To enable the production of caustic soda, etc., by efficiently subjecting salt water to electrolytic treatment even in the case that a new ion exchange membrane electrolytic cell reaction is started by previously treating the ion exchange membrane with a dilute caustic soda soln. specified in concn. before starting the electrolytic cell reaction after fixing the ion exchange membrane to the ion exchange membrane electrolytic cell. SOLUTION: The electrolytic cell 10 is divided into an anode chamber 2 and a cathode chamber 3 with the ion exchange membrane 1. An anode 4, a cathode 5 and the heater 6 for controlling an electrolytic temp. are arranged at these chambers. When the electrolytic cell 10 is energized and salt water is circulated to the anode chamber 2 and pure water is circulated to the cathode chamber 3, gaseous hydrogen and chlorine are recovered from the anode chamber 2 and the cathode chamber 3, and also the caustic soda is recovered as cathode chamber liq.. In such a case, when the electrolytic cell 10 is constructed by using the ion exchange membrane 1 subjected to dip treatment with dilute caustic soda soln., electrolytic voltage is kept low even at the start of the electrolytic cell 10 equipped with the new ion exchange membrane 1. Then the concn. of the caustic soda soln. is set to 1.0-3.0 wt.%.
    • 5. 发明专利
    • Ion exchange membrane electrolysis method
    • 离子交换膜电解法
    • JP2005126760A
    • 2005-05-19
    • JP2003362982
    • 2003-10-23
    • Chlorine Eng Corp Ltdクロリンエンジニアズ株式会社
    • HASHIMOTO TERUMIARIMOTO OSAMUKISHI TAKEMICHI
    • C02F1/46C25B9/00C25B15/00
    • PROBLEM TO BE SOLVED: To prevent the damage at the start of operating an ion exchange membrane fitted to an electrolytic cell in an ion exchange membrane electrolysis method.
      SOLUTION: In the ion exchange membrane electrolysis method, an ion exchange membrane is fitted to an ion exchange membrane electrolytic cell, thereafter, an alkali metal chloride aqueous solution having a concentration and a temperature in the range exhibiting an elongation percentage of -1.5 to 0% compared with the elongation in pure water at 25°C of the ion exchange membrane is filled into an anode chamber, and, after the completion of the change in the ion exchange membrane, the electrolytic liquid is exchanged with that having a concentration and a temperature at the time of regular operation.
      COPYRIGHT: (C)2005,JPO&NCIPI
    • 要解决的问题:为了防止在离子交换膜电解方法中操作安装在电解槽上的离子交换膜开始时的损伤。 解决方案:在离子交换膜电解方法中,将离子交换膜装配到离子交换膜电解槽中,然后将浓度和温度在伸长率的范围内的碱金属氯化物水溶液 与离子交换膜的25℃下的纯水中的伸长率相比为1.5〜0%,填充到阳极室中,在离子交换膜的变化完成后,将电解液与具有 浓度和正常运行时的温度。 版权所有(C)2005,JPO&NCIPI
    • 6. 发明专利
    • REDUCTION INHIBITIVE CATHODE AND ITS MANUFACTURE
    • JPH07252683A
    • 1995-10-03
    • JP4072594
    • 1994-03-11
    • CHLORINE ENG CORP LTD
    • ARIMOTO OSAMUKATAYAMA SHINJI
    • C25B9/10C25B1/26C25B1/28C25B11/20
    • PURPOSE:To prevent the reduction in yield through the cathodic reduction of a product from occurring by providing a layer contg. an ion exchanger on the surface of the cathode at the time of electrolyzing an inorganic salt aq. solution to produce a hypochlorite, chlorate, perchlorate or persulfate. CONSTITUTION:The reduction in production efficiency of a product through the reduction in current efficiency for electrolysis is caused by the cathodic reduction of e.g. the formed hypochlorite or chlorate ions to chloride ions at the time of electrolyzing an aq. solution of an inorganic salt such as sodium chloride, etc., to produce an oxidizing material such as hypochlorite, chlorate, perchlorate, persulfate, etc., or, by the cathodic reduction of persulfate ions to sulfate ions at the time of forming persulfate with electrolysis using a non- diaphragm process. In order to prevent this reduction in production efficiency, the cathode surface provided with porousness is coated with a cation exchanger when the ions to be reduced on the surface of the cathode are anions or, with an anion exchanger when the ions to be reduced on the surface of the cathode are cations, to prevent the reduction of the oxidizing material from occurring and to electrolytically produce the oxidizing material with high current efficiency and in a good yield.
    • 10. 发明专利
    • ACTIVE CATHODE ITS PRODUCTION AND ITS REGENERATING METHOD
    • JPH09324289A
    • 1997-12-16
    • JP16845096
    • 1996-06-07
    • CHLORINE ENG CORP LTD
    • KISHI TAKEMICHIARIMOTO OSAMU
    • C25B11/04
    • PROBLEM TO BE SOLVED: To provide an active cathode which is low in a manufacturing cost, is capable of maintaining a low hydrogen overvoltage, is simply and easily regeneratable in case of deterioration and degradation in its activity, maintains the initial high activity and is stably usable over long period of time even after the regeneration and is highly industrially practicable. SOLUTION: This active cathode is formed of a metallic base body, a first layer mainly composed of nickel of a high surface area on this material and a second layer mainly composed of rhodium of a high surface area of the cathode operation on this first layer. The metallic base body of this active cathode is preferably a nickel metal or nickel alloy. The cathode base body formed with the first layer mainly composed of the metallic nickel of the high surface area on the metallic base body is subjected to an immersion treatment in a rhodium salt-contg. soln. or is immersed into this rhodium salt-contg. soln. and is subjected to an electrolytic treatment with the cathode base body as cathode in the rhodium salt-contg. soln., by which the second layer mainly composed of the rhodium is formed on the first layer mainly composed of the nickel and the active cathode is thus produced.