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公开(公告)号:WO2015036591A1
公开(公告)日:2015-03-19
申请号:PCT/EP2014/069610
申请日:2014-09-15
Applicant: INDUSTRIE DE NORA S.P.A.
Inventor: BENEDETTO, Mariachiara , NISHIKI, Yoshinori
CPC classification number: C25B9/10 , C02F1/4618 , C02F1/4693 , C02F2001/46142 , C02F2001/46185 , C02F2201/46115 , C02F2201/4614 , C02F2201/46145 , C02F2209/06 , C25B1/26 , C25B9/08 , C25B11/03 , C25B11/0405 , C25B11/0415 , C25B11/0484 , C25B13/02 , C25B13/04 , C25B13/08 , C25B15/08
Abstract: The invention relates to a three-compartment electrolytic cell for production of oxidising disinfectant solutions. The intermediate compartment (300) of the cell is separated from the anodic compartment (200) by a fibrous diaphragm (321) in intimate contact with an anion-exchange membrane (320). The diaphragm (321) is formed by a network of organic polymer fibres mechanically bound to ceramic particles. The cathodic compartment (400) is separated from the intermediate compartment (300) by a cation-exchange membrane (340). Within intermediate compartment (300) a saturated solution of sodium chloride (510) is recycled. Inside tank (500) a decomposition catalyst is contained.
Abstract translation: 本发明涉及一种用于生产氧化消毒剂溶液的三室电解池。 电池的中间隔室(300)通过与阴离子交换膜(320)紧密接触的纤维隔膜(321)与阳极室(200)分离。 隔膜(321)由与陶瓷颗粒机械结合的有机聚合物纤维网形成。 阴极室(400)通过阳离子交换膜(340)从中间室(300)分离。 在中间室(300)内,再循环饱和氯化钠溶液(510)。 在内箱(500)内装有分解催化剂。
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公开(公告)号:WO2015014716A1
公开(公告)日:2015-02-05
申请号:PCT/EP2014/065948
申请日:2014-07-24
Applicant: INDUSTRIE DE NORA S.P.A.
Inventor: MANABE, Akiyoshi , NISHIKI, Yoshinori , KUNIMATSU, Akira
CPC classification number: C02F1/461 , B01D59/40 , C01B5/02 , C01B13/0207 , C02F2001/4619 , C02F2201/46185 , C25B1/04 , G21F9/007 , G21F9/08 , Y02E60/366
Abstract: An electrolytic enrichment method for heavy water includes enriching heavy water by electrolysis using an alkaline water electrolysis cell including an anode chamber that holds an anode, a cathode chamber that holds a cathode, and a diaphragm. In the method, an electrolyte prepared by adding high-concentration alkaline water to raw material water containing heavy water is circularly supplied to the anode chamber and the cathode chamber from a circulation tank; an anode-side gas-liquid separator and an anode-side water-seal device are connected to the anode chamber, and a cathode-side gas-liquid separator and a cathode-side water-seal device are connected to the cathode chamber; and electrolysis is continued while the alkali concentration in the electrolyte supplied to both electrolysis chambers is maintained at a constant concentration by circularly supplying, to the circulation tank, the electrolyte from which the gas generated from the anode-side gas-liquid separator and the cathode-side gas-liquid separator is separated.
Abstract translation: 用于重水的电解富集方法包括通过使用包括保持阳极的阳极室,保持阴极的阴极室和隔膜的碱性水电解池电解来富集重水。 在该方法中,通过向含有重水的原料水中添加高浓度碱性水而制备的电解质从循环罐向阳极室和阴极室循环供给; 阳极侧气液分离器和阳极侧水封装置连接到阳极室,阴极侧气液分离器和阴极侧水封装置连接到阴极室; 并且通过向循环罐循环供给从阳极侧气液分离器和阴极产生的气体的电解质,向供给到两个电解室的电解质中供给的电解质中的碱浓度保持恒定浓度,继续进行电解 侧气液分离器分离。
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