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    Water Electrolysis Treatment Device
    73.
    发明申请
    Water Electrolysis Treatment Device 审中-公开
    水电解处理装置

    公开(公告)号：US20130206671A1

    公开(公告)日：2013-08-15

    申请号：US13877198

    申请日：2011-10-12

    Applicant: Tomonori Ohira ,  Shinya Onoue ,  Kenji Kawashima

    Inventor： Tomonori Ohira ,  Shinya Onoue ,  Kenji Kawashima

    IPC: C02F1/469

    CPC classification number: C02F1/4695 ,  B01D61/422 ,  C02F1/4693 ,  C02F2001/46171 ,  C02F2101/20 ,  C02F2103/04 ,  C02F2103/08 ,  C02F2103/16 ,  C02F2201/003 ,  C02F2201/46115 ,  C02F2201/4617 ,  C02F2201/46185

    Abstract: A water electrolysis apparatus is provided that can stably produce water with high purity while preventing soiling and breakage, allows easy handling, detachment, and replacement, and allows inexpensive manufacture and maintenance. The water electrolysis apparatus includes: a treatment vessel; an anion cylinder having a cylindrical negative ion permeable membrane provided in the treatment vessel; a cation cylinder having a cylindrical positive ion permeable membrane provided in the treatment vessel; an anode provided in the cylindrical negative ion permeable membrane in an axial direction of the cylinder; and a cathode provided in the cylindrical positive ion permeable membrane in an axial direction of the cylinder, water to be treated stored in the treatment vessel can flow in an axial direction of the cylinder of the anion cylinder and the cation cylinder in the treatment vessel, and ion concentrated water with concentrated ions is obtained in the anion cylinder and the cation cylinder, and pure water is obtained in the treatment vessel.

    Abstract translation: 本发明提供一种能够稳定地生产高纯度的水，同时防止污染和破裂的水电解装置，易于处理，拆卸和更换，并且允许廉价的制造和维护。 水电解装置包括：处理容器; 设置在处理容器中的具有圆柱形负离子可渗透膜的阴离子筒; 具有设置在处理容器中的圆柱形正离子可渗透膜的阳离子筒; 设置在所述圆筒状的负离子透过膜中的在所述圆筒的轴向上的阳极; 以及设置在筒体的轴向的圆筒状的正离子透过膜中的阴极，储存在处理容器中的被处理水可以在处理容器内的阴离子筒和阳离子筒的筒体的轴向流动， 并且在阴离子筒和阳离子筒中获得具有浓缩离子的离子浓缩水，并且在处理容器中获得纯水。

    ELECTROCHEMICAL DIGESTION OF ORGANIC MOLECULES
    74.
    发明申请
    ELECTROCHEMICAL DIGESTION OF ORGANIC MOLECULES 审中-公开
    有机分子的电化学消解

    公开(公告)号：US20130087466A1

    公开(公告)日：2013-04-11

    申请号：US13630776

    申请日：2012-09-28

    Applicant: Robert Brian Dopp

    Inventor： Robert Brian Dopp

    IPC: B01D43/00 ,  C02F1/461 ,  C25B9/00 ,  C25B9/18 ,  C02F101/30

    CPC classification number: C02F1/4672 ,  C02F1/78 ,  C02F2001/46133 ,  C02F2101/30 ,  C02F2201/46175 ,  C02F2201/46185

    Abstract: Various methods and systems are provided for electrochemical digestion of organic molecules. In one example, among others, a method includes providing an electrolyte fluid including organic molecules between the electrodes of a reaction vessel and applying a voltage wave shape to the electrodes of the reaction vessel to digest the organic molecules. No separator exists between the electrodes of the reaction vessel. In another example, a system for digesting organic molecules includes a reaction vessel, an electrolyte fluid including the organic molecules, and a power source. The reaction vessel includes a plurality of electrodes where no separator exists between the electrodes. The electrolyte fluid is provided between the plurality of electrodes of the reaction vessel and the power source can applies a voltage wave shape to the electrodes of the reaction vessel to digest the organic molecules.

    Abstract translation: 提供了有机分子的电化学消解的各种方法和系统。 在一个实例中，其中包括在反应容器的电极之间提供包括有机分子的电解液，并将电压波形施加到反应容器的电极以消化有机分子。 在反应容器的电极之间不存在分离器。 在另一个实例中，用于消化有机分子的系统包括反应容器，包括有机分子的电解质流体和电源。 反应容器包括在电极之间不存在隔膜的多个电极。 电解质流体设置在反应容器的多个电极之间，电源可以向反应容器的电极施加电压波形以消化有机分子。

    Method for desalinating saltwater using concentration difference energy
    77.
    发明授权
    Method for desalinating saltwater using concentration difference energy 有权
    使用浓度差能量对盐水进行海水淡化的方法

    公开(公告)号：US08236158B2

    公开(公告)日：2012-08-07

    申请号：US12757382

    申请日：2010-04-09

    Applicant: Benjamin Stuart Sparrow ,  Joshua Aniket Zoshi ,  James Hing Bong Tang

    Inventor： Benjamin Stuart Sparrow ,  Joshua Aniket Zoshi ,  James Hing Bong Tang

    IPC: B01D61/44

    CPC classification number: C02F1/4693 ,  B01D61/025 ,  B01D61/145 ,  B01D61/147 ,  B01D61/50 ,  B01D61/54 ,  B01D61/58 ,  B01D2311/04 ,  B01D2311/2642 ,  B01D2313/36 ,  B01D2313/38 ,  B01D2317/02 ,  C02F1/004 ,  C02F1/04 ,  C02F1/041 ,  C02F1/048 ,  C02F1/16 ,  C02F1/24 ,  C02F1/32 ,  C02F1/441 ,  C02F1/444 ,  C02F1/447 ,  C02F1/4604 ,  C02F1/52 ,  C02F1/76 ,  C02F1/78 ,  C02F2001/007 ,  C02F2103/08 ,  C02F2201/009 ,  C02F2201/46115 ,  C02F2201/4613 ,  C02F2201/46145 ,  C02F2201/46185 ,  C02F2301/046 ,  C02F2301/08 ,  C02F2303/10 ,  H01M8/227 ,  Y02A20/128 ,  Y02A20/131 ,  Y02A20/134 ,  Y02A20/212 ,  Y02E60/50 ,  Y02W10/30 ,  Y02W10/37 ,  B01D2311/2649

    Abstract: Described herein are a method and system for desalinating saltwater using concentration difference energy. A “five stream” dialytic stack is described that can be used to desalinate saltwater at a relatively high recovery ratio. The dialytic stack may include, for example, one or more drive cells having a paired concentrate and a diluent-c chamber in ionic communication with a product chamber that is adjacent to an anion and a cation discharge chamber each filled with diluent-p. The drive cell applies a drive voltage across the product chamber, and when the drive voltage exceeds a desalination voltage of the product chamber, the saltwater in the product chamber is desalinated. The diluent-p may be at a lower ionic concentration than the diluent-c, which may be at a lower concentration than the concentrate. The relatively high concentrations of the concentrate and the diluent-c facilitate a relatively high recovery ratio, while the relatively low concentration of the diluent-p facilitates a relatively low desalination voltage. The dialytic stack may accept brine discharged from a first desalination plant and may use this brine as a source of the concentrate, diluent-c, or diluent-p. Alternatively, the dialytic stack may accept the brine as saltwater to be desalinated, and may then output desalinated brine back to the first desalination plant for further desalination. Processing the brine in the dialytic stack may decrease its volume, decreasing costs associated with treating or otherwise disposing of the brine.

    Abstract translation: 本文描述了使用浓度差能量使盐水脱盐的方法和系统。 描述了一种“五流”透析堆，可用于以相对高的回收率对盐水进行脱盐。 透析堆可以包括例如一个或多个驱动单元，其具有与阴离子相邻的产物室离子连通的成对浓缩物和稀释剂c室，每个充满稀释剂p的阳离子放电室。 驱动单元在产品室上施加驱动电压，当驱动电压超过产品室的脱盐电压时，产品室中的盐水脱盐。 稀释剂-p可以具有比稀释剂c更低的离子浓度，其可以具有比浓缩物更低的浓度。 浓缩物和稀释剂c的相对高的浓度有助于相对高的回收率，而稀释剂-p的相对较低的浓度便于相对较低的脱盐电压。 透析堆可以接收从第一个脱盐设备排出的盐水，并且可以使用该盐水作为浓缩物，稀释剂c或稀释剂-p的来源。 或者，透析堆可以接受盐水作为要脱盐的盐水，然后可以将脱盐盐水输出返回到第一脱盐设备以进一步脱盐。 处理透析塔中的盐水会降低其体积，降低与处理或以其他方式处置盐水相关的成本。

    ELECTROCHEMICAL DEVICE
    80.
    发明申请
    ELECTROCHEMICAL DEVICE 审中-公开
    电化学装置

    公开(公告)号：US20110189302A1

    公开(公告)日：2011-08-04

    申请号：US13056552

    申请日：2009-07-29

    Applicant: David-Lee Van Niekerk ,  Edmond O'Reilly ,  Kevin Keane ,  Eoin Croke ,  Michael Campion ,  Brendan Kennedy

    Inventor： David-Lee Van Niekerk ,  Edmond O'Reilly ,  Kevin Keane ,  Eoin Croke ,  Michael Campion ,  Brendan Kennedy

    IPC: C25B15/00 ,  C25B15/08 ,  A61K33/00 ,  A01P1/00

    CPC classification number: C25B15/02 ,  A01N59/00 ,  A61L2/035 ,  C02F1/4618 ,  C02F1/4674 ,  C02F2201/46125 ,  C02F2201/4618 ,  C02F2201/46185 ,  C02F2209/06 ,  C02F2303/04

    Abstract: There is provided an automated electrochemical device for generating a biocidal output solution, said device comprising: a flow-through electrochemical cell comprising an anodic chamber and a cathodic chamber for electrolysing an electrolyte to generate an anolyte solution and a catholyte solution; characterised in that the device further comprises: (i) a reservoir for storing catholyte; and (ii) a hydraulic circuit for recirculating catholyte from the reservoir to the anolyte on start-up of the cell, wherein input of catholyte of a compensating strength to the cell anodic chamber, is arranged so as to optimise the cell anolyte pH to produce a stable output solution at the start of the electrolysis process.

    Abstract translation: 提供了一种用于产生杀生物剂输出溶液的自动电化学装置，所述装置包括：流通电化学电池，包括阳极室和阴极室，用于电解电解质以产生阳极电解液和阴极电解液; 其特征在于，所述装置还包括：（i）用于存储阴极电解液的储存器; 和（ii）用于在电池启动时将阴极电解液从蓄液池再循环到阳极电解液的液压回路，其中输入具有对电解池阳极室的补偿强度的阴极电解液，以便优化细胞阳极电解液的pH以产生 在电解过程开始时稳定的输出溶液。

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