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    ELECTROCHEMICAL DIGESTION OF ORGANIC MOLECULES
    101.
    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。

    FLUID TREATMENT DEVICE
    103.
    发明申请
    FLUID TREATMENT DEVICE 审中-公开
    流体处理装置

    公开(公告)号：US20120261265A1

    公开(公告)日：2012-10-18

    申请号：US13479898

    申请日：2012-05-24

    Applicant: Eric John Kruger

    Inventor： Eric John Kruger

    IPC: B03C5/02

    CPC classification number: C02F1/4602 ,  C02F2103/023 ,  C02F2201/4611 ,  C02F2201/46125 ,  C02F2201/4613 ,  C02F2201/4615 ,  C02F2201/46175 ,  C02F2209/008 ,  C02F2209/05

    Abstract: A fluid treatment device is disclosed. The fluid treatment device includes at least a first electrode and a second electrode in direct contact with the fluid. The fluid treatment device may include a control device which adjusts a parameter of an alternating potential difference provided between the first electrode and the second electrode based on the indication of the conductivity between the first electrode and the second electrode.

    Abstract translation: 公开了一种流体处理装置。 流体处理装置至少包括与流体直接接触的第一电极和第二电极。 流体处理装置可以包括控制装置，其基于第一电极和第二电极之间的电导率的指示来调整设置在第一电极和第二电极之间的交替电位差的参数。

    Method integrating electrochemical oxidation and flocculation processes for pre-treatment of coking wastewater
    104.
    发明授权
    Method integrating electrochemical oxidation and flocculation processes for pre-treatment of coking wastewater 有权
    整合电化学氧化和絮凝过程的焦化废水预处理方法

    公开(公告)号：US08273249B2

    公开(公告)日：2012-09-25

    申请号：US12672112

    申请日：2008-07-25

    Applicant: Hongqiang Ren ,  Yunjun Yang ,  Lili Ding ,  Xiaolei Shi

    Inventor： Hongqiang Ren ,  Yunjun Yang ,  Lili Ding ,  Xiaolei Shi

    IPC: B01D21/00 ,  B01D21/01 ,  C02F1/52 ,  C02F1/72 ,  C02F1/461 ,  C02F1/00 ,  C02F1/34 ,  C02F1/48 ,  C02F1/76 ,  B03D3/00

    CPC classification number: C02F1/4608 ,  C02F1/5236 ,  C02F1/56 ,  C02F1/66 ,  C02F1/68 ,  C02F1/74 ,  C02F3/00 ,  C02F9/00 ,  C02F2001/46142 ,  C02F2101/30 ,  C02F2103/16 ,  C02F2201/46125 ,  C02F2201/46135 ,  C02F2201/4617 ,  C02F2201/46175 ,  C02F2209/44

    Abstract: A new method that integrates electrochemical oxidation and flocculation processes for removing ammonia nitrogen in coking wastewater is disclosed in this invention. It comprises steps as follow: first, adjusting the PH of coking wastewater and adding Fe2+ into the wastewater; then leading the wastewater containing Fe2+ through such 5 areas as pulsed high-voltage discharge oxidation area, pulsed high-frequency DC electrolytic oxidation area, microbubble oxidation area, flocculation area and precipitation area in succession. High-voltage pulse and high-frequency pulse are two different mechanisms for achieving strong oxidation. With help of both solid and liquid catalysts, these two oxidations can work synergistically. The recalcitrant organic chemicals are effectively destroyed and satisfactorily removed out of wastewater. The high-concentration coking waster pretreated with this method will meet Chinese highest discharge standard as long as the routine biochemical treatment is applied thereafter. The total investment on equipments and operation expenditure of the whole system is economically modest, which, together with its highly efficient treatment performance, ensures its extensive application in the field of wastewater treatment.

    Abstract translation: 在本发明中公开了一种将焦化废水中氨氮的电化学氧化和絮凝过程整合的新方法。 它包括以下步骤：首先调整焦化废水的PH值，​​并向废水中加入Fe2 +; 然后通过脉冲高压放电氧化区，脉冲高频直流电解氧化区，微泡氧化区，絮凝面积和沉淀面积等5个区域连续引导含有Fe2 +的废水。 高压脉冲和高频脉冲是实现强氧化的两种不同机制。 在固体和液体催化剂的帮助下，这两种氧化可以协同工作。 顽固的有机化学物质被有效地破坏，令人满意地从废水中除去。 用这种方法预处理的高浓度焦化废水，只要其后应用常规生化处理，将符合中国最高排放标准。 整个系统的设备投入和经营支出总体经济适用，加上高效的处理性能，确保了其在污水处理领域的广泛应用。

    HIGH-THROUGHPUT CAVITATION AND ELECTROCOAGULATION APPARATUS
    107.
    发明申请
    HIGH-THROUGHPUT CAVITATION AND ELECTROCOAGULATION APPARATUS 有权
    高强度渗透和电击装置

    公开(公告)号：US20110147231A1

    公开(公告)日：2011-06-23

    申请号：US12976253

    申请日：2010-12-22

    Applicant: Roman Gordon ,  Igor Gorodnitsky ,  Maxim A. Promtov

    Inventor： Roman Gordon ,  Igor Gorodnitsky ,  Maxim A. Promtov

    IPC: C02F1/463 ,  C25C7/00 ,  C25C7/06

    CPC classification number: C02F1/463 ,  C02F1/34 ,  C02F2001/46138 ,  C02F2001/46152 ,  C02F2103/08 ,  C02F2201/003 ,  C02F2201/4611 ,  C02F2201/4617 ,  C02F2201/46175

    Abstract: The invention relates to a cavitation and electrocoagulation reactor comprising a hollow cylindrical cathode having a cylindrical anode coaxially disposed therein to form an annular interelectrode gap between the contact surfaces. An inlet sleeve and an outlet sleeve disposed in the respective inlet and outlet of the cathode and abutting against opposite ends of the anode seal the interelectrode gap from the respective inlet and outlet of the cathode. A set of channels disposed in the wall of the inlet sleeve connect the inlet to the interelectrode gap. Similarly, a set of openings disposed in the outlet sleeve connect the interelectrode gap to the cathode outlet. An electrical source has first and second terminals respectively connected to the anode and the cathode. The method for removing contaminants from a contaminated fluid flow involves the simultaneous application of hydrodynamic cavitation and electrocoagulation to the contaminated fluid flow.

    Abstract translation: 本发明涉及一种空化和电凝反应器，包括一个中空圆柱形阴极，其圆柱形阳极同轴地设置在其中，以在接触表面之间形成环形的电极间间隙。 设置在阴极的相应入口和出口处并与阳极的相对端抵接的入口套筒和出口套筒将电极间隙与阴极的相应入口和出口密封。 设置在入口套筒的壁中的一组通道将入口连接到电极间间隙。 类似地，设置在出口套筒中的一组开口将电极间间隙连接到阴极出口。 电源具有分别连接到阳极和阴极的第一和第二端子。 从被污染的流体流中除去污染物的方法涉及将水动力空化和电凝同时施加到受污染的流体流。

    TUBULAR ELECTROLYSIS CELL AND CORRESPONDING METHOD
    110.
    发明申请
    TUBULAR ELECTROLYSIS CELL AND CORRESPONDING METHOD 有权
    管状电解质细胞和相应方法

    公开(公告)号：US20090314659A1

    公开(公告)日：2009-12-24

    申请号：US12488360

    申请日：2009-06-19

    Applicant: Bruce F. Field

    Inventor： Bruce F. Field

    IPC: G01N27/26

    CPC classification number: C02F1/4618 ,  A47L11/4041 ,  C02F2001/46133 ,  C02F2001/46152 ,  C02F2001/46161 ,  C02F2201/003 ,  C02F2201/4611 ,  C02F2201/46115 ,  C02F2201/46125 ,  C02F2201/46175 ,  C02F2201/4618

    Abstract: An electrolysis cell is provided, which includes an inlet, an outlet, and coaxial, cylindrical inner and outer electrodes. A cylindrical ion-selective membrane is located between the inner and outer electrodes and forms respective first and second electrolysis reaction chambers on opposing sides of the membrane. Fluid flow paths along the first and second chambers join together as a combined inlet flow path through the inlet and a combined outlet flow path through the outlet.

    Abstract translation: 提供一种电解池，其包括入口，出口和同轴的圆柱形内外电极。 圆柱形离子选择膜位于内电极和外电极之间，并在膜的相对侧上形成相应的第一和第二电解反应室。 沿着第一和第二腔室的流体流动路径通过穿过入口的组合的入口流动路径和通过出口的组合的出口流动路径连接在一起。

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