Electrodeionization apparatus
    61.
    发明申请
    Electrodeionization apparatus 失效
    电离电离装置

    公开(公告)号:US20050098436A1

    公开(公告)日:2005-05-12

    申请号:US11015797

    申请日:2004-12-20

    CPC classification number: B01D61/52 B01D61/48 B01J47/08 C02F1/4695 Y02A20/134

    Abstract: An electrodeionization apparatus in which enough electric current flows even when the voltage applied between the electrodes is low, thereby sufficiently performing deionization is provided. A single first cation exchange membrane 3, a single anion exchange membrane 4, a single second cation exchange membrane 3′ are arranged between a cathode 1 and an anode 2 so that a concentration-cathode compartment 5, a desalting compartment 7, a concentrating compartment 10, and an anode compartment 6 are formed, in this order, between the cathode 1 and the anode 2. The concentration-cathode compartment 5 and the anode compartment 6 are filled with a cation exchange resin 8, respectively. The desalting compartment 7 is filled with a mixture of the cation exchange resin 8 and an anion exchange resin 9. Fed into the anode compartment 6 is raw water or deionized water. Water from the anode compartment is sent to the concentrating compartment 10 and the concentration-cathode compartment 5 sequentially.

    Abstract translation: 即使在施加在电极之间的电压低的情况下,也能够充分地进行去离子化的电离电离装置。 在阴极1和阳极2之间设置单个第一阳离子交换膜3,单个阴离子交换膜4,单个第二阳离子交换膜3',使得浓缩阴极室5,脱盐室7,浓缩室 依次形成阴极1和阳极2之间的阳极室6。 浓阴极室5和阳极室6分别用阳离子交换树脂8填充。 脱盐室7填充有阳离子交换树脂8和阴离子交换树脂9的混合物。 进入阳极室6的是原水或去离子水。 来自阳极室的水顺序送入浓缩室10和浓阴极室5。

    Electrodeionization apparatus having geometric arrangement of ion
exchange material
    62.
    发明授权
    Electrodeionization apparatus having geometric arrangement of ion exchange material 失效
    具有离子交换材料几何排列的电离离子装置

    公开(公告)号:US6156180A

    公开(公告)日:2000-12-05

    申请号:US142242

    申请日:1998-07-13

    CPC classification number: B01D43/00 B01D61/48 B01J47/007 B01J47/08 C02F1/4695

    Abstract: An electrodeionization apparatus adapted to remove ions from a liquid, the apparatus having a cathode proximate a first end of the apparatus and an anode proximate the opposite end of the apparatus and having a plurality of alternating diluting compartments and concentrating compartments positioned between the cathode and the anode, the diluting and concentrating compartments defined by anion and cation permeable membranes, and ion exchange material positioned within the diluting compartments, the diluting compartments having therein a continuous phase of a first ion exchange material containing a dispersed phase of clusters of a second ion exchange material. The method of removing ions from a liquid in such an electrodeionization apparatus comprises passing an aqueous liquid to be purified through the diluting compartments in which the diluting compartments have the continuous phase of a first ion exchange material with the dispersed phase of a second ion exchange material.

    Abstract translation: PCT No.PCT / CA97 / 00018 Sec。 371日期1998年8月21日 102(e)1998年8月21日PCT PCT 1997年1月13日PCT公布。 公开号WO97 / 25147 日期1997年7月17日一种用于从液体中去除离子的电去离子装置,该装置具有靠近装置的第一端的阴极和靠近装置的相对端的阳极,并且具有多个交替的稀释隔室和集中隔室 在阴极和阳极之间,由阴离子和阳离子可渗透膜定义的稀释和浓缩隔室以及位于稀释隔室内的离子交换材料,其中具有连续相的第一离子交换材料含有分散相的簇 的第二离子交换材料。 在这种电去离子装置中从液体中除去离子的方法包括将要净化的水性液体通过稀释室,其中稀释室具有第一离子交换材料的连续相,其中第二离子交换材料的分散相 。

    Electrodialysis apparatus
    63.
    发明授权
    Electrodialysis apparatus 失效
    电渗析仪

    公开(公告)号:US6117297A

    公开(公告)日:2000-09-12

    申请号:US283742

    申请日:1999-04-01

    Abstract: An integral, monolithic frame-membrane is disclosed, such frame-membrane having a semi-permeable membrane portion and integral therewith a frame portion, the frame portion having one or more cavities, each cavity juxtaposed to the membrane portion, each cavity having at least one fluid entrance conduit communicating with an entrance manifold aperture and at least one fluid exit conduit communicating with an exit manifold aperture. The integral, monolithic frame-membrane may be used in apparatus for carrying out gas-separation; microfiltration; ultrafiltration; nanofiltration; reverse osmosis (i.e. hyperfiltration); diffusion dialysis; Donnan dialysis; electrodialysis (including filled-cell electrodialysis; i.e. electrodeionization); pervaporation; piezodialysis; membrane distillation; osmosis; thermo osmosis; and electrolysis with membranes. Also disclosed are pillows prepared from ion exchanging films or fabrics (which may be porous or non-porous), the pillows filled with ion exchange structures such as beads, fibers, fabrics or rods. The pillows may be used with the integral, monolithic frame-membranes, with separate frames and membranes or with frames only.

    Abstract translation: 公开了一种整体的整体框架膜,这种框架膜具有半透膜部分并与框架部分成一体,框架部分具有一个或多个空腔,每个空腔与膜部分并置,每个空腔至少具有 一个与入口歧管孔连通的流体入口导管和与出口歧管孔连通的至少一个流体出口管。 集成的整体框架膜可用于进行气体分离的设备中; 微滤; 超滤; 纳滤; 反渗透(即过滤); 扩散透析; 唐南透析 电渗析(包括填充电池电渗析,即电去离子化); 渗透蒸发 压力透析 膜蒸馏; 渗透 热渗透; 并用膜电解。 还公开了由离子交换膜或织物(其可以是多孔或无孔)制备的枕头,枕头填充有离子交换结构,例如珠,纤维,织物或棒。 枕头可以与整体的整体框架膜一起使用,具有单独的框架和隔膜,或仅与框架一起使用。

    Robust technetium removal method and system
    64.
    发明授权
    Robust technetium removal method and system 失效
    强大的锝去除方法和系统

    公开(公告)号:US5954936A

    公开(公告)日:1999-09-21

    申请号:US818484

    申请日:1997-03-14

    CPC classification number: C01G99/003 B01J47/04 B01J47/08

    Abstract: The invention provides a method and processing system for removing both anionic and cationic technetium complexes from an aqueous solution by adjusting the pH of the solution to greater than approximately 2, and directing the solution into an integrated resin and electrochemical plating device. The integrated resin and plating device has a resin bed or resin membrane in which is disposed one or more cathodes, and one or more anodes. A potential generator produces at least a 1 volt potential between the cathodes and the anodes. As the solution passes through the resin, the technetium complexes are adsorbed onto it. When a sufficient concentration of technetium complexes is adsorbed, the plating process can atlernatively be driven to plate out the technetium onto the cathodes, or to collect various species in system anolytes/catholytes.

    Abstract translation: 本发明提供了一种方法和处理系统,用于通过将溶液的pH调节至大约2,从而将水溶液中的阴离子和阳离子锝络合物除去,并将溶液引导到一体化树脂和电化学电镀装置中。 集成树脂和电镀装置具有树脂床或树脂膜,其中设置有一个或多个阴极和一个或多个阳极。 电位发生器在阴极和阳极之间产生至少1伏的电位。 当溶液通过树脂时,锝络合物被吸附在其上。 当吸附足够浓度的锝络合物时,电镀过程可以被驱赶,将锝沉积到阴极上,或者在系统的阳极液/阴极液中收集各种物质。

    Electrolytic cell arrangement for the deionization of aqueous solutions
    65.
    发明授权
    Electrolytic cell arrangement for the deionization of aqueous solutions 失效
    用于水溶液去离子的电解槽排列

    公开(公告)号:US5954935A

    公开(公告)日:1999-09-21

    申请号:US756986

    申请日:1996-11-26

    Abstract: In an electrochemical cell arrangement for the deionization of aqueous solutions by ion exchange including cathode and anode chambers having electrodes disposed therein, a brine chamber is disposed between, and directly adjacent to, the cathode and anode chambers which are filled with anion and cation exchanger materials such that the electrodes are directly in contact therewith and means are provided for conducting the aqueous solution to be treated through the cathode and anode chambers and means for passing brine through the brine chamber to be charged therein by the ions removed from the aqueous solution in the cathode and anode chambers.

    Abstract translation: 在用于通过离子交换去离子水溶液的电化学电池装置中,包括具有设置在其中的电极的阴极室和阳极室,盐水室设置在阴极室和阳极室之间,并且与阴极和阳离子交换材料 使得电极直接与其接触,并且提供用于通过阴极和阳极室传导待处理水溶液的装置和用于使盐水通过盐水室的装置,以通过在水溶液中从在水溶液中除去的离子 阴极和阳极室。

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