METHOD FOR PRODUCING OXIDIZED WATER FOR STERILIZATION USE WITHOUT ADDING ELECTROLYTE
    5.
    发明申请
    METHOD FOR PRODUCING OXIDIZED WATER FOR STERILIZATION USE WITHOUT ADDING ELECTROLYTE 有权
    用于生产氧化水的方法用于灭菌,不加电解质

    公开(公告)号:US20160272514A1

    公开(公告)日:2016-09-22

    申请号:US15037382

    申请日:2014-12-08

    发明人: Osao SUMITA

    IPC分类号: C02F1/461 C02F1/42

    摘要: A method for producing oxidized water for sterilization use which contains chlorine dioxide, said method comprising: electrolyzing tap water containing chlorine ions using a three-chamber-type electrolysis vessel, in which an intermediate chamber is located between an anode chamber and a cathode chamber; trapping the chlorine ions dissolved in the tap water; and electrolytically oxidizing the trapped chlorine ions on an anode electrode. A partitioning membrane that isolates the anode chamber from the intermediate chamber is composed of a fluorine-containing cation exchange membrane and an anion exchange membrane, wherein a porous anode electrode is adhered onto the fluorine-containing cation exchange membrane in the partitioning membrane. A partitioning membrane that isolates the cathode chamber from the intermediate chamber is composed of a cation exchange membrane or an anion exchange membrane, wherein a porous cathode electrode is adhered onto the partitioning membrane; and an anion exchange resin is filled in the intermediate chamber.

    摘要翻译: 一种生产包含二氧化氯的灭菌用氧化水的方法,所述方法包括:使用三室型电解容器对含有氯离子的自来水进行电解,其中中间室位于阳极室和阴极室之间; 捕获自来水中溶解的氯离子; 并在阳极上电解氧化被捕获的氯离子。 将阳极室与中间室隔离的分隔膜由含氟阳离子交换膜和阴离子交换膜构成,其中多孔阳极电极附着在分隔膜中的含氟阳离子交换膜上。 将阴极室与中间室隔离的分隔膜由阳离子交换膜或阴离子交换膜构成,其中多孔阴极粘合到分隔膜上; 并且阴离子交换树脂填充在中间室中。

    DESALINATION AND PURIFICATION SYSTEM
    10.
    发明申请
    DESALINATION AND PURIFICATION SYSTEM 有权
    脱盐净化系统

    公开(公告)号:US20140318972A1

    公开(公告)日:2014-10-30

    申请号:US14325423

    申请日:2014-07-08

    IPC分类号: C02F1/469

    摘要: A liquid electrolyte can be desalinated and purified using a system that includes a first electrode and a configuration selected from (a) a second electrode and at least one distinct ion-selective boundary and (b) a second electrode that also serves as the ion-selective boundary. The ion-selective boundary is contained in the liquid conduit adjacent to a porous medium that defines pore channels filled with the liquid and that have a surface charge, and the charge of the ion-selective boundary and the surface charge of the pore channels share the same sign. A liquid including at least one charged species flows through the pore channels, forming a thin diffuse electrochemical double layer at an interface of the liquid and the charged surface of the pore channels. A voltage differential is applied between the electrodes across the porous medium to draw ions in the liquid to the electrodes to produce brine at the electrodes and to create a shock in the dissolved-ion concentration in the bulk volume of the liquid within the pore channels, wherein a depleted zone with a substantially reduced concentration of dissolved ions forms in the liquid bulk volume between the shock and the ion-selective boundary.

    摘要翻译: 可以使用包括第一电极和选自(a)第二电极和至少一个不同的离子选择性边界的构造的系统对液体电解质进行脱盐和纯化,以及(b)也用作离子交换膜的第二电极, 选择性边界。 离子选择性边界包含在与多孔介质相邻的液体管道中,该多孔介质限定填充有液体的孔隙通道,并且具有表面电荷,并且孔隙通道的离子选择性边界和表面电荷的电荷共享 相同的标志。 包含至少一种带电荷的物质的液体流过孔道,在液体和孔道的带电表面的界面处形成薄的漫射电化学双层。 在电极之间穿过多孔介质施加电压差以将液体中的离子吸引到电极以在电极处产生盐水并且产生在孔隙通道内的液体的体积体积中的溶解离子浓度的冲击, 其中在冲击和离子选择性边界之间的液体本体体积中形成具有基本上降低的溶解离子浓度的贫化区。