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    • 1. 发明授权
    • Apparatus for electrochemical decontamination of radioactive metallic
waste
    • 放射性金属废物电化学去污设备
    • US5865965A
    • 1999-02-02
    • US786931
    • 1997-01-23
    • Masami EndaJiro SakuraiHitoshi SakaiOsamu Sasaki
    • Masami EndaJiro SakuraiHitoshi SakaiOsamu Sasaki
    • G21F9/00C25B9/00C25B11/02C25B11/03
    • G21F9/004
    • An insulating shield plate (1) divides a room of an electrolysis bath (2) into an anode chamber (13) and a cathode chamber (14). An anode (5) is disposed in the anode chamber (13), and a cathode (6), metallic waste (7) and heater (4) are disposed in the cathode chamber (14). An electrolyte (3) stored in the electrolysis bath (2) flows in a circulation path from a circulating pump (10) through a circulating line (12) and filter (11) to return the electrolysis bath (2). An exhaust gas processing device 9 is connected to the electrolysis bath (2). When a voltage is supplied to the anode (5) and cathode (6), a surface of the metallic waste (7) is charged in a positive polarity to dissolve a base metal of the metallic waste (7). Further, a cylindrical anode (33) is arranged in an electrolyte (32) in an electrolysis bath (31), and a cylindrical metal (34) as a metallic waste is arranged in the cylindrical anode (33). After a bar-shaped cathode (35) is arranged in the cylindrical metal (34), a DC voltage is supplied to the cylindrical anode (33) and the bar-shaped cathode (35). At this time, the system may be constructed in that oxygen occurs by charging in a positive polarity in an inner surface of the cylindrical metal (34) and the base metal of the cylindrical shape is dissolved.
    • 绝缘屏蔽板(1)将电解槽(2)的室分成阳极室(13)和阴极室(14)。 阳极(5)设置在阳极室(13)中,阴极(6),金属废物(7)和加热器(4)设置在阴极室(14)中。 存储在电解槽(2)中的电解液(3)从循环泵(10)通过循环管线(12)和过滤器(11)的循环路径流动,使电解槽(2)返回。 排气处理装置9与电解槽(2)连接。 当向阳极(5)和阴极(6)供应电压时,金属废物(7)的表面以正极性充电以溶解金属废物(7)的基底金属。 此外,在电解槽(31)中的电解质(32)中配置有圆筒状的阳极(33),在圆筒状的阳极(33)上配置作为金属废料的圆筒状金属(34)。 在圆柱形金属(34)中设置棒状阴极(35)之后,向圆筒形阳极(33)和棒状阴极(35)供给直流电压。 此时,可以构造系统,其中通过在圆柱形金属(34)的内表面中以正极性充电而发生氧,并且圆柱形的基体金属被溶解。
    • 3. 发明授权
    • Method of chemically decontaminating components of radioactive material handling facility and system for carrying out the same
    • 化学去除放射性物质处理设备的组成部分的方法及其执行方法
    • US06635232B1
    • 2003-10-21
    • US09468906
    • 1999-12-22
    • Yumi YaitaMasami EndaHitoshi Sakai
    • Yumi YaitaMasami EndaHitoshi Sakai
    • G21C1900
    • C25B1/13C25B9/10G21F9/002G21F9/004
    • Ozone gas having a high ozone concentration is generated by a solid electrolyte electrolytic process. An ozone solution is prepared by injecting the ozone gas into an acidic solution of pH 6 or below. The ozone solution heated at a temperature in the range of 50° to 90° C. is supplied to a contaminated object to oxidize and dissolve a chromium oxide film by an oxidizing dissolving process. The ozone solution used in the oxidizing dissolving process is irradiated with ultraviolet rays to decompose ozone contained in the ozone solution, the ozone solution is passed through an ion-exchange resin to remove ions contained in the ozone solution. An oxalic acid solution is supplied to the contaminated object to dissolve an iron oxide film by a reductive dissolving process. Oxalic acid remaining in the oxalic acid solution after the reduction dissolving process is decomposed by injecting ozone into the oxalic acid solution and irradiating the oxalic acid solution with ultraviolet rays, and ions contained in the oxalic acid solution is removed by an ion-exchange resin.
    • 通过固体电解质电解法生成臭氧浓度高的臭氧气体。 通过将臭氧气体注入pH6以下的酸性溶液中制备臭氧溶液。 在50〜90℃的温度范围内加热的臭氧溶液被供给到污染物,通过氧化溶解法氧化和溶解氧化铬膜。 在氧化溶解过程中使用的臭氧溶液用紫外线照射以分解臭氧溶液中所含的臭氧,臭氧溶液通过离子交换树脂以除去臭氧溶液中所含的离子。 向被污染物质供给草酸溶液,通过还原溶解法溶解氧化铁膜。 在还原溶解工序后残留在草酸溶液中的草酸通过将臭氧注入草酸溶液中并用紫外线照射草酸溶液而分解,并且通过离子交换树脂除去草酸溶液中所含的离子。
    • 6. 发明授权
    • Method of chemically decontaminating components of radioactive material handling facility and system for carrying out the same
    • 化学去除放射性物质处理设备的组成部分的方法及其执行方法
    • US06875323B2
    • 2005-04-05
    • US10645593
    • 2003-08-22
    • Yumi YaitaMasami EndaHitoshi Sakai
    • Yumi YaitaMasami EndaHitoshi Sakai
    • B08B3/00C25B11/04C25D17/00G21F9/00
    • C25B1/13C25B9/10G21F9/002G21F9/004
    • Ozone gas having a high ozone concentration is generated by a solid electrolyte electrolytic process. An ozone solution is prepared by injecting the ozone gas into an acidic solution of pH 6 or below. The ozone solution heated at a temperature in the range of 50° to 90° C. is supplied to a contaminated object to oxidize and dissolve a chromium oxide film by an oxidizing dissolving process. The ozone solution used in the oxidizing dissolving process is irradiated with ultraviolet rays to decompose ozone contained in the ozone solution, the ozone solution is passed through an ion-exchange resin to remove ions contained in the ozone solution. An oxalic acid solution is supplied to the contaminated object to dissolve an iron oxide film by a reductive dissolving process. Oxalic acid remaining in the oxalic acid solution after the reductive dissolving process is decomposed by injecting ozone into the oxalic acid solution and irradiating the oxalic acid solution with ultraviolet rays, and ions contained in the oxalic acid solution is removed by an ion-exchange resin.
    • 通过固体电解质电解法生成臭氧浓度高的臭氧气体。 通过将臭氧气体注入pH6以下的酸性溶液中制备臭氧溶液。 在50〜90℃的温度下加热的臭氧溶液被供给到被污染的物体,通过氧化溶解法氧化和溶解氧化铬膜。 在氧化溶解过程中使用的臭氧溶液用紫外线照射以分解臭氧溶液中所含的臭氧,臭氧溶液通过离子交换树脂以除去臭氧溶液中所含的离子。 向被污染物质供给草酸溶液,通过还原溶解法溶解氧化铁膜。 在还原性溶解过程中残留在草酸溶液中的草酸通过将臭氧注入草酸溶液中并用紫外线照射草酸溶液而分解,并且通过离子交换树脂除去草酸溶液中所含的离子。
    • 7. 发明授权
    • Apparatus and method for electrochemical decontamination of radioactive
metallic waste
    • 放射性金属废物的电化学去污设备和方法
    • US5877388A
    • 1999-03-02
    • US870450
    • 1997-06-06
    • Masami EndaKatsumi HosakaHitoshi SakaiHideaki Heki
    • Masami EndaKatsumi HosakaHitoshi SakaiHideaki Heki
    • G21F9/00G21F9/06G21F9/30A62D3/00C25B9/00C25D17/00
    • G21F9/06G21F9/004G21F9/30
    • An insulating shield plate (1) divides a room of an electrolysis bath (2) into an anode chamber (13) and a cathode chamber (14). An anode (5) is disposed in the anode chamber (13), and a cathode (6), metallic waste (7) and heater (4) are disposed in the cathode chamber (14). An electrolyte (3) stored in the electrolysis bath (2) flows in a circulation path from a circulating pump (10) through a circulating line (12) and filter (11) to return the electrolysis bath (2). An exhaust gas processing device 9 is connected to the electrolysis bath (2). When a voltage is supplied to the anode (5) and cathode (6), a surface of the metallic waste (7) is charged in a positive polar to dissolve a base metal of the metallic waste (7). Further, a cylindrical anode (33) is arranged in an electrolyte (32) in an electrolysis bath (31), and a cylindrical metal (34) as a metallic waste is arranged in the cylindrical anode (33). After a bar-shape cathode (35) is arranged in the cylindrical metal (34), a DC voltage is supplied to the cylindrical anode (33) and the bar-shape cathode (35). At this time, the system may be constructed in that oxygen occurs by charging in a positive polarity an inner surface of the cylindrical metal (34) and the base metal of the cylindrical shape is dissolved.
    • 绝缘屏蔽板(1)将电解槽(2)的室分成阳极室(13)和阴极室(14)。 阳极(5)设置在阳极室(13)中,阴极(6),金属废物(7)和加热器(4)设置在阴极室(14)中。 存储在电解槽(2)中的电解液(3)从循环泵(10)通过循环管线(12)和过滤器(11)循环通道返回电解槽(2)。 排气处理装置9与电解槽(2)连接。 当向阳极(5)和阴极(6)供应电压时,金属废物(7)的表面以正极被充电以溶解金属废物(7)的母材。 此外,在电解槽(31)中的电解质(32)中配置有圆筒状的阳极(33),在圆筒状的阳极(33)上配置作为金属废料的圆筒状金属(34)。 在圆柱形金属(34)中布置棒状阴极(35)之后,向圆筒形阳极(33)和棒状阴极(35)供给直流电压。 此时,可以构造系统,其中通过以正极性的方式对圆柱形金属(34)的内表面进行充电并且圆柱形的基底金属溶解而发生氧。