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    • 2. 发明授权
    • End plate for a metal gas cell
    • 金属气室的端板
    • US5002842A
    • 1991-03-26
    • US465694
    • 1990-01-16
    • Vincent J. PuglisiGuy G. RampeKenneth R. RichardsonOrville G. Prickett
    • Vincent J. PuglisiGuy G. RampeKenneth R. RichardsonOrville G. Prickett
    • H01M2/02H01M10/34
    • H01M10/345H01M2/0255
    • A support assembly, including an end plate, for use in metal gas cells. The support assembly inhibits a plate stack which is positioned within a pressure vessel from impinging the walls of the pressure vessel. The support assembly comprises a first and a second weld ring and a first and a second end plate, each of the end plates being attached to a different end of the plate stack. The first and second weld rings mate with the first and second end plates, respectively, and cooperate to support the plate stack. The end plate comprises two plates secured together. A raised portion on one of the plates forming the end plate has a radially extending embossment formed therein to increase the rigidity thereof. The pressure vessel is constructed of generally cylindrical container defining two circumferentially extending lips, each of which is secured to an end portion.
    • 一种用于金属气体池的支撑组件,包括端板。 支撑组件抑制位于压力容器内的板堆撞击压力容器的壁。 支撑组件包括第一和第二焊接环以及第一和第二端板,每个端板附接到板堆叠的不同端部。 第一和第二焊接圈分别与第一和第二端板配合,并配合以支撑板堆叠。 端板包括固定在一起的两个板。 形成端板的一个板上的凸起部分具有形成在其中的径向延伸的压花以增加其刚度。 压力容器由通常为圆柱形的容器构成,限定两个周向延伸的唇缘,每个唇缘固定到端部。
    • 5. 发明授权
    • Method of making sintered plaque nickel electrodes
    • 制造烧结斑块镍电极的方法
    • US4292143A
    • 1981-09-29
    • US126640
    • 1980-03-03
    • Harvey N. SeigerVincent J. Puglisi
    • Harvey N. SeigerVincent J. Puglisi
    • H01M4/29H01M4/32H01M4/80H01M10/44C25D11/00
    • H01M4/29H01M4/32H01M4/80
    • The improved method of the invention comprises electrochemically depositing nickel hydroxide into the pores of a clean sintered nickel plaque cathode from heated aqueous electrolyte at acid pH in a treating zone containing an anode, while minimizing corrosion of the plaque. The electrochemical deposition is continued only until a loading level of about 2 grams per cubic centimeter of void volume in the plaque is obtained. This is in order to avoid thickening, swelling and stressing of the plaque. The method is carried out without the need for a wetting agent in the electrolyte. The plaque should be sufficiently clean so as to be readily wetted throughout by the electrolyte. Such a clean condition can be produced by heating the plaque to at least about 700.degree. C. Plaque corrosion is minimized by polarizing the plaque cathode as by the use of a sacrificial cadmium cathode. Plaque corrosion can also be minimized by maintaining an electric current in the electrolyte whenever the plaque is present therein. It is preferred to carry out the deposition while applying a substantially constant level of current to the electrodes. Loading levels of nickel hydroxide in excess of 7.7 ampere hours per cubic inch can be effected for an improved product.
    • 本发明的改进方法包括在含有阳极的处理区中将氢氧化镍电化学沉积在酸性pH下的加热的含水电解质的清洁的烧结镍斑块阴极的孔中,同时最小化斑块的腐蚀。 电化学沉积继续进行,直到得到斑块中约2克/立方厘米空隙体积的负载水平。 这是为了避免斑块的增厚,肿胀和压力。 该方法在电解质中不需要润湿剂的情况下进行。 斑块应足够清洁,以便易于被电解液润湿。 这样一个干净的条件可以通过将该板加热到至少约700℃来产生。通过使用牺牲镉阴极使斑块阴极极化,使得斑块腐蚀最小化。 当斑块存在于其中时,通过保持电解质中的电流也可以最小化斑块腐蚀。 优选在对电极施加大致恒定电流的电流的同时进行沉积。 可以对改进的产品进行氢氧化镍的装载量超过7.7安培小时/立方英寸。
    • 8. 发明授权
    • Rechargeable lead-hydrogen electrochemical cell
    • 可充电铅氢电池
    • US4467020A
    • 1984-08-21
    • US459841
    • 1983-01-21
    • Vincent J. Puglisi
    • Vincent J. Puglisi
    • H01M12/08H01M4/86H01M10/34
    • H01M4/86H01M10/345
    • An improved rechargeable lead-hydrogen electrochemical cell is provided which comprises a cell stack secured to a retainer and disposed within a pressure vessel containing hydrogen gas. The stack includes a positive electrode comprising lead oxide, a pair of gas-porous negative electrodes containing a catalyst, a pair of separators and a pair of gas screens. The stack components are saturated with sulfuric acid electrolyte. Each of the negative electrodes has a separator disposed on one side thereof and a gas screen disposed on the opposite side thereof. The pressure vessel contains a gas inlet, and electrical leads connect to, respectively, the positive and negative electrodes and exit the pressure vessel. In the charged form, the cell reactants exist as lead oxide and hydrogen gas. When the cell is discharged, the lead oxide is reduced to lead sulfate and the hydrogen gas is oxidized at a catalytic surface to hydrogen ion. The cell has a lower cost with fewer technical problems, has a higher specific energy density and has a superior performance, relative to conventional metal hydrogen cells.
    • 提供了一种改进的可充电铅氢电化学电池,其包括固定到保持器并设置在包含氢气的压力容器内的电池堆。 堆叠包括包含氧化铅的正电极,含有催化剂的一对气体多孔负极,一对隔板和一对气体屏蔽。 堆叠组分用硫酸电解质饱和。 每个负极具有设置在其一侧的隔膜和设置在其相对侧上的气体屏蔽。 压力容器包含气体入口,电引线分别连接正极和负极并离开压力容器。 在带电形式中,电池反应物作为氧化铅和氢气存在。 当电池放电时,氧化铅被还原为硫酸铅,氢气在催化剂表面被氧化成氢离子。 相对于常规金属氢电池,电池具有更低的成本,更少的技术问题,具有更高的比能量密度并且具有优异的性能。