公开(公告)号：US20040232007A1

公开(公告)日：2004-11-25

申请号：US10492017

申请日：2004-04-08

Inventor： Roger W Carson ,  Bruce W Bremer

IPC: C25F005/00 ,  C02F001/461

CPC classification number: C02F1/4672 ,  A61L2/035 ,  A61L11/00 ,  C02F1/32 ,  C02F1/36 ,  C02F1/46104 ,  C02F2103/22 ,  C02F2103/26 ,  C02F2103/32 ,  C02F2201/46115 ,  C02F2201/4612 ,  C02F2201/46155 ,  C02F2201/46185 ,  C02F2305/026

Abstract: A mediated electrochemical oxidation process is used to treat, oxidize and destroy food waste materials, such as manure, biological residue, hay, straw, animal byproducts, bones, horns, blood, biological items, pathological waste and combined waste. Food waste is introduced into an apparatus for contacting the waste with an electrolyte containing the oxidized form of one or more reversible redox couples, at least one of which is produced by anodic oxidation in an electrochemical cell. The oxidized species of the redox couples oxidize the organic waste molecules and are themselves converted to their reduced form, whereupon they are reoxidized by either of the aforementioned mechanisms and the redox cycle continues until all oxidizable waste species, including intermediate reaction products, have undergone the desired degree of oxidation. The process takes place at temperatures between zero degrees centigrade and below the boiling point of the electrolyte.

Abstract translation: 介导的电化学氧化方法用于处理，氧化和破坏食品废物，如肥料，生物残渣，干草，秸秆，动物副产品，骨头，角，血液，生物制品，病理废物和混合废物。 将食物废物引入用于使废物与含有一种或多种可逆的氧化还原对的氧化形式的电解质接触的装置，其中至少一种是在电化学电池中通过阳极氧化制备的。 氧化还原对的氧化物质氧化有机废物分子，并将其自身转化为还原形式，由此上述两种机制再次氧化，氧化还原循环持续到包括中间反应产物在内的所有可氧化废物已经经历了 所需的氧化程度。 该过程发生在零摄氏度和低于电解质沸点的温度下。

公开(公告)号：US20040188258A1

公开(公告)日：2004-09-30

申请号：US10484446

申请日：2004-01-21

Inventor： Yohei Takahashi ,  Kunio Fujiwara ,  Takayoshi Kawamoto ,  Syu Nakanishi ,  Toru Akiyama ,  Masaji Akahori ,  Jun Aoyama

IPC: B01D061/44

CPC classification number: C02F1/4695 ,  B01D61/44 ,  B01D61/48 ,  B01D61/52 ,  B01D65/08 ,  B01D2321/16 ,  B01J47/08 ,  C02F1/42 ,  C02F2201/46115 ,  C02F2201/46185

Abstract: The object of the present invention is to provide an electrical deionization apparatus capable of long-term operation at a low voltage. To achieve this object, the present invention is directed to an electrical deionization apparatus based on a completely new compartment configuration and provides an electrical deionization apparatus comprising multiple compartments separated by cation- and anion-exchange membranes arranged between anode and cathode, wherein the anion-exchange membrane on the anode side and the cation-exchange membrane on the cathode side together define a water splitting compartment, and wherein an anion deionization compartment defined between anion-exchange membranes is placed on the anode side of the water splitting compartment, and a cation deionization compartment defined between cation-exchange membranes is placed on the cathode side of the water splitting compartment.

Abstract translation: 本发明的目的是提供能够在低电压下长期运行的电去离子装置。 为了实现这个目的，本发明涉及一种基于全新隔室结构的去离子电气设备，并且提供一种电去离子设备，其包括由布置在阳极和阴极之间的阳离子交换膜和阴离子交换膜隔开的多个室， 阳极侧的交换膜和阴极侧的阳离子交换膜一起形成水分离室，其中阴离子交换膜之间限定的阴离子去离子室被放置在分水室的阳极侧，阳离子 限定在阳离子交换膜之间的去离子室被放置在分水室的阴极侧。

公开(公告)号：US20030010639A1

公开(公告)日：2003-01-16

申请号：US10203988

申请日：2002-08-15

Inventor： L. Karl Legatski ,  Eric M. Legatski

IPC: B01D035/06 ,  C02F001/40 ,  C25B009/00 ,  C02F011/00 ,  C25B011/00 ,  C25B013/00 ,  F25B041/02 ,  B01D061/42 ,  B01D069/00 ,  B01D071/00 ,  B01D061/46 ,  B01D061/52

CPC classification number: C25D13/24 ,  B01D61/145 ,  B01D61/422 ,  B01D61/44 ,  B01D61/46 ,  B01D61/54 ,  B01D61/58 ,  C02F1/444 ,  C02F1/469 ,  C02F9/00 ,  C02F2103/14 ,  C02F2201/003 ,  C02F2201/46115 ,  C02F2201/46185 ,  C25D21/22

Abstract: An electrodialysis cell (40) suitable for removal of paint solubilizer from electrocoat paint ultrafilter permeate includes a tubular, non-conductive housing (42), a substantially cylindrical, hollow object electrode (48) in the housing, a substantially cylindrical counter electrode (52) situated within the hollow object electrode, and a tubular ion exchange membrane (50) around the counter electrode but spaced from the counter electrode as well as the object electrode. The counter electrode and the tubular membrane together define an annular electrolyte passageway while the object electrode and the tubular membrane together define an annular ultrafilter permeate passageway. The object electrode-to-counter electrode area ratio is at least about 6.

Abstract translation: 适用于从电涂漆超滤膜渗透物去除涂料增溶剂的电渗析池（40）包括管状非导电壳体（42），壳体中基本为圆柱形的中空物体电极（48），大致圆柱形的对电极（52 ）和位于对电极周围但与对电极以及物体电极隔开的管状离子交换膜（50）。 对电极和管状膜一起限定环形电解质通道，同时物体电极和管状膜一起限定环形超滤膜渗透通道。 对象电极对电极面积比至少约为6。

公开(公告)号：US20020036134A1

公开(公告)日：2002-03-28

申请号：US09852243

申请日：2001-05-09

Inventor： Kazuhiro Shirota ,  Akira Isaka

IPC: C25B009/00

CPC classification number: A61L2/18 ,  A61L2/035 ,  C02F1/4618 ,  C02F2001/4619 ,  C02F2201/4611 ,  C02F2201/46115 ,  C02F2201/4612 ,  C02F2201/46145 ,  C02F2201/4618 ,  C02F2201/46185 ,  C02F2209/006 ,  C02F2209/02 ,  C02F2209/04 ,  C02F2209/06 ,  C02F2303/04

Abstract: A manufacturing method and apparatus of strongly alkaline ionized water exceeding pH 12.0 by electrolysis of water. As an electrolysis solution supplied to a cathode cell of an electrolytic bath, alkaline ionized water produced in the cathode cell is used, and an operation, in which the alkaline ionized water produced in the cathode cell is circulated and supplied to the cathode cell and is subjected to application of electrolytic voltage, is repeated, so that a cation is accumulated to increase the pH value. As a method for circulating and supplying the alkaline ionized water produced in the cathode cell to the cathode cell, a circulation container bath is used, and the circulation container bath and the cathode cell of the electrolytic bath are connected via a circulating line containing a circulating pump. The circulation container bath has a withdrawing system containing a water collecting device for withdrawing alkaline ionized water having a desired pH value to the outside.

Abstract translation: 强碱性电离水的制造方法和装置，通过水电解超过pH12.0。 作为向电解槽的阴极单元供给的电解液，使用在阴极单元中产生的碱性电离水，将在阴极单元中产生的碱性离子水循环供给至阴极单元的工序， 重复施加电解电压，使得积累阳离子以增加pH值。 作为将阴极单元中产生的碱性电离水循环供给到阴极单元的方法，使用循环容器槽，电解槽的循环容器槽和阴极单元通过循环管线连接， 泵。 循环容器槽具有抽出系统，该抽出系统含有用于将具有所需pH值的碱性离子水向外部排出的集水装置。

公开(公告)号：US6117285A

公开(公告)日：2000-09-12

申请号：US838252

申请日：1997-04-17

Applicant: William D. Welch ,  Daniel L. Robinson

Inventor： William D. Welch ,  Daniel L. Robinson

IPC: A61C19/00 ,  A61L2/00 ,  A61L2/03 ,  A61L2/18 ,  C02F1/00 ,  C02F1/461 ,  C02F1/467 ,  C02F1/78 ,  C25B15/00 ,  C25B9/00

CPC classification number: A61L2/183 ,  A61L2/0011 ,  A61L2/035 ,  C02F1/46104 ,  C02F1/4674 ,  A61C19/002 ,  A61L2202/24 ,  C02F1/4672 ,  C02F1/78 ,  C02F2001/46133 ,  C02F2001/46138 ,  C02F2001/46142 ,  C02F2001/46152 ,  C02F2103/026 ,  C02F2201/4612 ,  C02F2201/46185 ,  C02F2301/024 ,  C02F2303/04

Abstract: An apparatus for electrolyzing fluids. The resulting electrolyzed fluids are particularly suited for treating physiological materials such as whole blood, plasma, or cell isolates in order to reduce the effect of harmful microorganisms. A container holds the fluid and a power supply provides a source of electrical current to an anode and a cathode positioned within the container. The system is particularly suited for disinfecting and/or sterilizing health care instruments. The instruments are bathed in the electrolyzed saline solution. If the instrument includes internal conduits the system of the present invention also preferably flows the electrolyzed saline solution through such conduits also to provide both cleaning and sterilization. The electrolyzed saline solution is recirculated from the electrodes to the instrument being sterilized. Embodiments of the invention are particularly suited to sterilizing dental drill handpieces without damage to the handpieces.

Abstract translation: 一种用于电解液体的装置。 所得的电解液特别适合于治疗全血，血浆或细胞分离物等生理材料，以减少有害微生物的作用。 容器保持流体，并且电源向位于容器内的阳极和阴极提供电流源。 该系统特别适用于消毒和/或消毒保健仪器。 将仪器沐浴在电解盐水溶液中。 如果仪器包括内部导管，本发明的系统还优选地通过这种导管使电解盐水溶液流动，以提供清洁和灭菌。 电解盐水溶液从电极再循环到被灭菌的仪器上。 本发明的实施例特别适用于在不破坏手机的情况下对牙钻手机进行消毒。

公开(公告)号：US5968337A

公开(公告)日：1999-10-19

申请号：US984222

申请日：1997-12-02

Applicant: Jeffrey E. Surma ,  Norvell Nelson ,  G. Anthony Steward ,  Garry H. Bryan

Inventor： Jeffrey E. Surma ,  Norvell Nelson ,  G. Anthony Steward ,  Garry H. Bryan

IPC: A62D3/00 ,  A62D3/11 ,  A62D3/13 ,  A62D3/36 ,  A62D3/38 ,  A62D101/02 ,  A62D101/06 ,  A62D101/22 ,  A62D101/26 ,  A62D101/28 ,  B01D53/46 ,  B01D53/72 ,  B01F11/02 ,  C02F1/36 ,  C02F1/461 ,  C02F1/467 ,  C02F1/72 ,  C25B3/02

CPC classification number: A62D3/11 ,  B01D53/72 ,  C02F1/36 ,  C02F1/46104 ,  C02F1/4672 ,  C02F1/72 ,  A62D2101/02 ,  A62D2101/06 ,  A62D2203/10 ,  C02F2101/003 ,  C02F2101/30 ,  C02F2101/32 ,  C02F2201/46115 ,  C02F2201/4612 ,  C02F2201/46155 ,  C02F2201/46185 ,  C02F2305/026

Abstract: The invention is a method and apparatus using high cerium concentration in the anolyte of an electrochemical cell to oxidize organic materials. The method and apparatus further use an ultrasonic mixer to enhance the oxidation rate of the organic material in the electrochemical cell. A reaction vessel provides an advantage of independent reaction temperature control and electrochemical cell temperature control. A separate or independent reaction vessel may be used without an ultrasonic mixer to oxidize gaseous phase organic materials.

Abstract translation: 本发明是在电化学电池的阳极电解液中使用高铈浓度以氧化有机材料的方法和装置。 该方法和装置还使用超声波混合器来增强电化学电池中的有机材料的氧化速率。 反应容器提供独立的反应温度控制和电化学电池温度控制的优点。 可以使用独立或独立的反应容器，而不需要超声波混合器来氧化气相有机材料。

公开(公告)号：US4121991A

公开(公告)日：1978-10-24

申请号：US705710

申请日：1976-07-15

Applicant: Jorge Miller ,  Franz Stummer

Inventor： Jorge Miller ,  Franz Stummer

IPC: C02F1/00 ,  C02F1/461 ,  C02B1/82 ,  B01D13/02 ,  C02C5/12

CPC classification number: C02F1/46114 ,  C02F1/46104 ,  C02F2001/46152 ,  C02F2201/003 ,  C02F2201/4611 ,  C02F2201/46185 ,  C02F2301/024

Abstract: The specification describes an electrolytic cell for the treatment, particularly the purification and sterilization of water, which comprises a closed container with a lower inlet opening and an upper outlet opening for the water and electrodes which are adapted to be connected with the positive pole and the negative pole of a DC source. In the interior of the electrolytic cell free movable particles are located whose density is higher than that of the water to be treated and which are prevented from leaving the electrolytic cell by suitable means adajcent to the inlet and the outlet.

Abstract translation: 该说明书描述了用于处理的电解池，特别是水的净化和灭菌，其包括具有下入口和用于水和电极的上出口开口的封闭容器，其适于与正极和 直流电源的负极。 在无电解池的可移动颗粒的内部，其密度高于被处理水的密度，并且通过适合于入口和出口的手段而被阻止离开电解槽。

公开(公告)号：US3869364A

公开(公告)日：1975-03-04

申请号：US32133373

申请日：1973-01-05

Applicant: VAST ASSOCIATES INC J

Inventor： TEJEDA ALVARO R

IPC: B01D61/52 ,  C02F1/42 ,  C02F1/46 ,  C02F1/469 ,  B01K5/00

CPC classification number: B01D61/52 ,  C02F1/42 ,  C02F1/4604 ,  C02F1/469 ,  C02F2201/46115 ,  C02F2201/46185

Abstract: An electrodialytic cell in which electrochemical corrosion of a ferrous anode electrode is inhibited by including said electrode as a wall portion of an anode electrode chamber, of which another spaced wall portion constitutes a permselective membrane, and by sweeping the anode electrode chamber with a water solution containing a hydroxide of a cation selected from the group consisting of sodium, potassium, lithium, cesium, rubidium and ammonium.

Abstract translation: 一种电渗析池，其中通过将所述电极作为阳极电极室的壁部分包括所述电极而被抑制，其中另一间隔壁部分构成选择性渗透膜，并且通过用水溶液扫掠阳极电极室 含有选自钠，钾，锂，铯，铷和铵的阳离子的氢氧化物。

公开(公告)号：US20240317614A1

公开(公告)日：2024-09-26

申请号：US18368974

申请日：2023-09-15

Applicant: Clear World Corporation

Inventor： Boris Davidoff ,  Johannes Verwater

IPC: C02F1/467 ,  C02F1/461

CPC classification number: C02F1/4674 ,  C02F1/46109 ,  C02F2001/46133 ,  C02F2001/46171 ,  C02F2201/4612 ,  C02F2201/46175 ,  C02F2201/46185 ,  C02F2209/29 ,  C02F2301/024 ,  C02F2303/04

Abstract: A chemical reactor unit is provided that includes first and second circulation loops and an anode arranged between the first and second circulation loops. A first cathode is located at a beginning of the first circulation loop and a second cathode is located at an end of the second circulation loop. The chemical reactor unit can be used to generate a chlorine dioxide solution. A method for generating a chlorine dioxide solution includes applying a voltage differential between first and second cathodes and an anode arranged therebetween and pumping a fluid mixture comprising sodium chlorite and oxalic acid to sequentially pass the first cathode, the anode, and the second cathode. An apparatus is additional provided that includes a tank configured to hold a fluid mixture, a chemical reactor unit, and a pump configured to circulate the fluid mixture between the tank and the chemical reactor unit.

公开(公告)号：US11661357B2

公开(公告)日：2023-05-30

申请号：US16286418

申请日：2019-02-26

Applicant: Z Intellectual Property Holding Company, LLC

Inventor： Gaylord M. Karren ,  James K. Stone ,  John M. Hopkins ,  William R. Shupe

IPC: B08B3/10 ,  B08B3/04 ,  C02F1/461 ,  C02F1/48 ,  B08B3/08 ,  C02F1/00 ,  A61L2/18 ,  C25F1/00 ,  C25B1/04 ,  C25B9/73 ,  A47L11/40 ,  C25B15/02 ,  C25B9/19 ,  A47L11/34 ,  C02F103/02

CPC classification number: C02F1/4618 ,  A61L2/18 ,  B08B3/04 ,  B08B3/08 ,  B08B3/10 ,  C02F1/008 ,  C02F1/46109 ,  C02F1/48 ,  C02F1/481 ,  C25B1/04 ,  C25F1/00 ,  A47L11/34 ,  A47L11/4005 ,  A47L11/4044 ,  A47L11/4075 ,  A47L11/4086 ,  A61L2202/11 ,  C02F1/005 ,  C02F2001/4619 ,  C02F2001/46185 ,  C02F2103/026 ,  C02F2201/008 ,  C02F2201/4611 ,  C02F2201/4612 ,  C02F2201/4614 ,  C02F2201/4619 ,  C02F2201/46115 ,  C02F2201/46125 ,  C02F2201/46135 ,  C02F2201/46145 ,  C02F2201/46185 ,  C02F2201/48 ,  C02F2209/003 ,  C02F2209/05 ,  C02F2209/40 ,  C02F2209/42 ,  C02F2301/026 ,  C02F2301/046 ,  C02F2303/04 ,  C02F2303/22 ,  C25B9/19 ,  C25B9/73 ,  C25B15/02 ,  Y02E60/36

Abstract: The present invention relates to systems and methods for cleaning materials, such as flooring and upholstery. In some cases, the systems and methods use an electrolytic cell to electrolyze a solution comprising sodium carbonate, sodium bicarbonate, sodium acetate, sodium percarbonate, potassium carbonate, potassium bicarbonate, and/or any other suitable chemical to generate electrolyzed alkaline water and/or electrolyzed oxidizing water. In some cases, the cell comprises a recirculation loop that recirculates anolyte through an anode compartment of the cell. In some cases, the cell further comprises a senor and a processor, where the processor is configured to automatically change an operation of the cell, based on a reading from the sensor. In some cases, a fluid flows past a magnet before entering the cell. In some additional cases, fluid from the cell is conditioned by being split into multiple conduits that run in proximity to each other. Additional implementations are described.