公开(公告)号：US20050072665A1

公开(公告)日：2005-04-07

申请号：US10480412

申请日：2002-06-14

Applicant: Rodolfo Gomez

Inventor： Rodolfo Gomez

IPC: A61L2/02 ,  A61L2/03 ,  C02F1/461 ,  C25B15/00

CPC classification number: A61L2/035 ,  A61L2/02 ,  C02F1/46104 ,  C02F1/4618 ,  C02F2001/46138 ,  C02F2201/46155 ,  C02F2201/46195 ,  C02F2209/06 ,  C02F2303/04

Abstract: A unipolar liquid activation apparatus with an anode cell (40), a cathode cell (41), and a direct current power supply (43), the anode cell having an anode (46), a liquid inlet (50) and an anolyte outlet (51), the cathode cell having a cathode (47), a liquid inlet (52) and a catholyte outlet (53), means to electrically connect the anode and cathode respectively to the direct current power supply. The cells can also include connected solution electrodes (44, 49). Alternatively the anode and cathode can be compound electrodes (81, 83) with means to electrically connect the inner anode electrode and the inner cathode electrode. The anode cell and cathode cell may be adjacent to each other and electrically connected by an electronic membrane (104) in contact respectively with the anode and cathode and allowing flow of electrons only from the cathode to the anode. The unipolar activation apparatus may also be an anode (141) and a cathode (142) electrically isolated from each other but connected to a DC power source.

Abstract translation: 具有阳极单元（40），阴极单元（41）和直流电源（43）的单极液体激活装置，所述阳极单元具有阳极（46），液体入口（50）和阳极电解液出口 （51），具有阴极（47），液体入口（52）和阴极电解液出口（53）的阴极单元，分别将阳极和阴极电连接到直流电源。 电池还可以包括连接的溶液电极（44,49）。 或者，阳极和阴极可以是具有电连接内部阳极电极和内部阴极电极的装置的复合电极（81,83）。 阳极单元和阴极单元可以彼此相邻并且通过分别与阳极和阴极接触的电子膜（104）电连接并允许电子仅从阴极流到阳极。 单极激活装置也可以是彼此电隔离但连接到直流电源的阳极（141）和阴极（142）。

公开(公告)号：US20050196656A1

公开(公告)日：2005-09-08

申请号：US11005556

申请日：2004-12-06

Applicant: Rodolfo Gomez

Inventor： Rodolfo Gomez

IPC: H01M4/86 ,  H01M4/92 ,  H01M8/02 ,  H01M8/10 ,  H01M8/24

CPC classification number: H01M4/86 ,  H01M4/8626 ,  H01M4/92 ,  H01M8/02 ,  H01M8/0276 ,  H01M8/10 ,  H01M8/1004 ,  H01M8/1016 ,  H01M8/24 ,  H01M8/241 ,  H01M2008/1095 ,  H01M2250/20 ,  H01M2300/0094 ,  Y02E20/16 ,  Y02E60/521 ,  Y02T90/32

Abstract: A process and apparatus to modify the conventional proton exchange fuel cell by applying a non-conductive proton exchange material (5), a separate semiconductor (8), cylindrical-conical fuel cell elements (1,3), and internally stacking the fuel cell elements by a simple method. These modifications in the operating principle and construction configuration of the proton exchange fuel cell are designed to result in a major increase in the power density output necessary for transport vehicle and stationary power generation applications.

Abstract translation: 一种通过施加非导电质子交换材料（5），单独的半导体（8），圆柱形锥形燃料电池元件（1,3）来改变常规质子交换燃料电池并在内部堆叠燃料电池的方法和装置 元素通过简单的方法。 质子交换燃料电池的工作原理和结构配置中的这些修改被设计成导致运输车辆和固定发电应用所需的功率密度输出的显着增加。

公开(公告)号：US5882502A

公开(公告)日：1999-03-16

申请号：US710983

申请日：1996-09-25

Applicant: Rodolfo Gomez

Inventor： Rodolfo Gomez

IPC: C22B3/04 ,  C25C1/00 ,  C25C1/08 ,  C25C1/12 ,  C25C1/20 ,  C25C5/02 ,  C25C7/00 ,  C25C7/06 ,  C25C7/04

CPC classification number: C22B11/04 ,  C22B3/045 ,  C25C1/00 ,  C25C1/12 ,  C25C1/20 ,  C25C5/02 ,  C25C7/00 ,  C25C7/002 ,  C25C7/06 ,  Y02P10/234

Abstract: An electrochemical apparatus and system for extracting and recovering metals from their compounds using electrochemical cells where the anolyte 10 is connected electrically to the catholyte 11 through an independent set of electrodes 13, 14 immersed in each electrolyte and connected to each other by a conductor 16. The specification details the application of this principle to commercial size cells and systems to extract metals from solutions, from ores in-situ, from ores in heaps and fixed beds, from fine metal concentrates dissolved either at the anode cell or in a separate leaching vessel. Alkaline electrolytes are also given for the extraction and recovery of nickel and copper from their oxide ores. A method for extracting gold from ores or residues is also included.

Abstract translation: 一种用于使用电化学电池从其化合物中提取和回收金属的电化学装置和系统，其中阳极电解液10通过浸在每个电解质中并通过导体16彼此连接的独立的一组电极13,14电连接到阴极电解液11。 该规范详细说明了该原理应用于商业尺寸的电池和系统，从溶液，原位矿石，堆和固定床中的矿石中提取金属，从在阳极电池中溶解的细金属浓缩物或单独的浸出容器 。 还提供碱性电解质用于从其氧化物矿石中提取和回收镍和铜。 还包括从矿石或残渣中提取黄金的方法。