• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A bipolar electrode element has an electrically conductive, chemically inert, generally flat wall having first and second opposing faces, each of the first and second faces having a plurality of spaced, parallel grooves therein with the spaced grooves in the first face being laterally staggered from the spaced grooves in the second face, first and second spaced and substantially parallel electrodes having first edges disposed within first and second respective grooves of said spaced parallel grooves in said first face and extending generally perpendicular from the plane of the inert wall; and a third electrode having a first edge disposed within a groove in said second face and extending generally perpendicular from the plane of the inert wall. A battery stack is obtained by positioning a plurality of the bipolar battery elements such that their electrodes are interdigitated.
    公开号:SU1284465A3
    申请号:SU782584748
    申请日:1978-02-22
    公开日:1987-01-15
    发明作者:Карр Питер
    申请人:Энерджи Девелопмент Ассошиэйтс,Инк (Фирма)；
    IPC主号:
    专利说明:

    -

    R
    SP

    s
    The invention relates to chemical current sources and relates to a battery of metal-halogen cells.
    The purpose of the invention is to eliminate short circuits by reducing the formation of dendrites.
    FIG. 1 shows the proposed battery metal-halogen elements, a general view; Fig 2 is the same cross section.
    Each battery cell contains a neutral, electrically conductive flat wall 1J which has first 2 and second 3 opposite sides. The plane of the first side 2 is parallel to the plane of the second side 3. On the side 2 are grooves 4, which are; parallel to each other and preferably arranged symmetrically on side 2.
    Similarly, grooves 5 are made on side 3, which are parallel to each other and are preferably arranged symmetrically on side 3, grooves 4 of side 2 are arranged in a staggered order relative to yaz 5 of side 3, and it is preferable that each groove 5 is in the middle not below a pair of adjacent grooves 4 and vice versa .
    Wall 1 can be made of any suitable electrically conductive material that is chemically resistant, i.e., chemically neutral to electrolyte and other chemicals with which it will contact.
    In addition, the wall 1 may be made of graphite or metal. It is desirable that the wall is impermeable to electrolyte and gases. One edge of the electrodes 6, for example, zinc is located in the corresponding grooves 4 on side 2 of wall 1 so that electrode 6 is in electrical contact with wall 1,
    One edge of the electrodes 7 is located in the corresponding slots 5 on the side 3 of the wall 1. In the battery: metal-halogen elements, the electrode 7 is a halogen electrode and can be made of any suitable electrode material such as porous graphite or porous noble catalyzed metal.
    The edges of the electrodes 6 in the corresponding grooves 4 and the edges of the electrodes 7 in: the corresponding grooves b are held by appropriate means. For example, Kra can


    held by cementing, staggered at the point of contact or by welding. However, it is preferable to make the electrodes so that they are slightly thicker than the corresponding grooves so that their edges are inserted into the grooves under pressure and held in place by a tight fit. A dense fit of the electrodes into the corresponding grooves is simple and easy to carry out and gives a small contact resistance,
    The chlorine electrodes 7 are made so that they have an internal cavity 8. Such a structure can be made by known methods, for example by making two halves of the appropriate shape, which are then fastened along the edges or through a non-conductive stable film, or fitted and bonded electrode halves directly between themselves.
    Cavity 8 is the space that is filled with electrolyte. Electrode 7 is also provided with gas passage holes. In order to achieve uniform distribution of electrolyte in each individual chlorine electrode 7, the chlorine electrode is supplied with electrolyte through a thin tube 9 connected to an upstream pipeline system and acting as a flow regulating nozzle. It is advisable that the tubes 9 supply the electrolyte from the conduit 10 down to the bottom of the cavity 8 of the chlorine electrode, since it is necessary that the electrolyte flow to the bottom of the cell. Such a device also minimizes input parasitic currents by increasing the tube length for maximum electrolyte input resistance. The electrolyte is supplied to conduit 10 from reservoir 11.
    The inert wall 1 of each bipolar element is located parallel to the wall 1 of adjacent bipolar elements.
    Chlorine electrodes 7 of one bipolar element are moved with zinc electrodes 6 of an adjacent bipolar element. Each electrode extends almost to the neutral wall of the adjacent bipolar electrode element so that it is between the edge of the electrode and the neutral wall 1.
    the adjacent bipolar element has only a small gap.
    The electrodes between each pair of adjacent neutral walls 1 form a cell, the area of which can be increased simply by extending the neutral wall 1 and attaching additional electrodes .. At the same time, the electrodes at the borders of each cell are either all zinc 6 or chloric 7. Such a device limits the external closure, as it provides a potential difference across the cell width equal to half the potential difference that occurs when the external electrodes alternate from zinc 6 to chlorine 7 along the entire battery.
    According to FIG. 2 separate bipolar elements are located on a suitable insulating stable substrate 12 of the cell. The neutral walls 1 are attached to the substrate by any suitable means, for example clamps, with through titanium bolts on a glass substrate. For better fastening, you can use a porous Teflon gasket between the glass and the bipolar element. With this configuration, the walls of the battery consist of the extreme neutral walls, i.e. walls that have electrodes on only one side, and external electrodes in each individual cell. Since there is a small gap between the edge of each electrode and its neighboring neutral wall, a suitable neutral gasket 13 is placed in the gap at its outer electrode. There is no cover, so that each electrode in the battery is open to the gas collection space, which provides the best gas output possible from the cell. If the battery is placed in a case, there must be adequate gas space at the top.
    In the case of long-term cell action, it is necessary to provide space for collecting metallic sludge. As shown in FIG. .1, this can be accomplished by mounting the electrodes so that there is little space between the bottom of the electrodes and the bottom of the neutral wall 1. However, in order to maintain the electrolyte in the cell, the external electrodes must necessarily reach the bottom and be attached to an insulating substrate, for example, to a porous teflok pad on the substrate.
    Neutral walls, which are inserted as cell dividers, are made slightly above the tips of the electrodes in the cell. The electrical insulation between the cells is provided by the high resistance of the electrolyte film flowing through the edge of the electrode or the inner wall.
    The proposed battery may contain 10-12 bipolar comb-type cells. Each element can have a neutral wall 1 with a height of 10 cm and a length of 12 cm. Each first surface 2 can have 14 zinc electrode 6, protruding 6.35 - 8 cm from the plane of surface 2 and the top edge lying 2.54 cm below the upper edge of the neutral wall t.
    Each second surface 3 may have 12 chlorine electrodes 7 protruding 6.35 - 8 cm from the plane of surface 3, with the upper edge of each being 2.54 cm lower than the edge of the neutral wall 1, and the lower edge of each being 0.3 cm higher than the lower edges of the neutral wall 1. The bottom edge of each zinc electrode 6, with the exception of the external electrodes 6, may be 0.3 cm above the bottom edge of the neutral wall t.
    Thus, the effective inter-cell distance, which is determined by the distance between the neutral walls of 6.35 - 8 cm, is much larger than the actual interelectrode distance, whereby the reduction of the parasitic and / or dendritic effects occurring in the electrochemical battery
    权利要求:
    Claims (1)
    [1]
    Invention Formula
    A battery of metal-halogen bipolar, elements arranged in parallel and containing an electrically conductive neutral wall with opposite polar electrode pitastins on opposite sides, so that, in order to eliminate short circuits by reducing the formation of dandrites, neutral walls are located on 6.35 - 8.0 cm from each other and on both sides in grooved order, grooves are made to place 512844656
    In them, perpendicular to the wall, those electrode plates with one field, p, with one edge of the corresponding electrodes, are located between electrode plates, and in each element plate of the other polarity.
    /
    1g
    Vll. g
    类似技术:
    公开号 | 公开日 | 专利标题
    SU1284465A3|1987-01-15|Battery of metal-halogen bipolar cells
    CA1130854A|1982-08-31|Shunt current elimination in electrochemicaldevices
    US4551399A|1985-11-05|Bipolar battery
    US4648955A|1987-03-10|Planar multi-junction electrochemical cell
    US3833424A|1974-09-03|Gas fuel cell battery having bipolar graphite foam electrodes
    US6524453B1|2003-02-25|Electrode assembly
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    US3953238A|1976-04-27|Multicell seawater battery
    US4675254A|1987-06-23|Electrochemical cell and method
    US4382849A|1983-05-10|Apparatus for electrolysis using gas and electrolyte channeling to reduce shunt currents
    GB1233177A|1971-05-26|
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    US4416953A|1983-11-22|Secondary battery
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    JPH1069917A|1998-03-10|Fuel cell
    EP0127616A1|1984-12-12|Plural cell storage battery
    US987717A|1911-03-28|Electrolytic cell.
    US1360545A|1920-11-30|Isaac h
    RU66864U1|2007-09-27|BLOCK-PLANAR ELEMENT AND PACKAGE BASED ON THESE ELEMENTS
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    US2806077A|1957-09-10|Core wound battery
    JPS57175950A|1982-10-29|Micro-flow cell type voltammetry detector
    SU574794A1|1977-09-30|Fluid-tight accumulator
    US1651989A|1927-12-06|Active-material support for storage cells
    同族专利:
    公开号 | 公开日
    DE2806962A1|1978-08-24|
    DE2806962B2|1980-12-04|
    IT1101973B|1985-10-07|
    JPS63174168U|1988-11-11|
    IT7848115D0|1978-02-20|
    FR2381398A1|1978-09-15|
    SE442254B|1985-12-09|
    CA1092646A|1980-12-30|
    CH629036A5|1982-03-31|
    JPH0429493Y2|1992-07-16|
    ES467192A1|1979-08-16|
    PL116452B1|1981-06-30|
    US4100332A|1978-07-11|
    JPS53121134A|1978-10-23|
    BR7801033A|1978-10-10|
    MX144178A|1981-09-08|
    DE2806962C3|1982-07-08|
    BE864217A|1978-06-16|
    NL7802004A|1978-08-24|
    PL204822A1|1978-10-23|
    SE7801988L|1978-08-23|
    FR2381398B1|1983-09-23|
    GB1594752A|1981-08-05|
    引用文献:
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    GB185946A|1921-08-31|1922-09-21|John Robert Palmer|Improvements in electric accumulators|
    US3167456A|1961-06-01|1965-01-26|Gen Motors Corp|Battery|
    US3316167A|1961-09-01|1967-04-25|Exxon Research Engineering Co|Multi-cell reactor in series|
    US3592695A|1968-11-01|1971-07-13|Gen Electric|Metal-air cell including a composite laminar gas diffusion cathode|
    US3575720A|1969-02-03|1971-04-20|Gen Motors Corp|Insulator means for lithium-chlorine high temperature battery|
    US3728158A|1971-11-16|1973-04-17|Gen Motors Corp|Low silhouette bi-polar battery|
    JPS526704B2|1971-11-25|1977-02-24|
    US3855002A|1973-12-21|1974-12-17|United Aircraft Corp|Liquid electrolyte fuel cell with gas seal|DE3041386C2|1980-11-03|1983-04-28|Energy Development Associates Inc., 48071 Madison Heights, Mich.|Electrode arrangement of a collector|
    US4343982A|1981-03-23|1982-08-10|Energy Development Associates, Inc.|Method of joining metal to graphite by spot welding|
    US4382113A|1981-03-23|1983-05-03|Energy Development Associates, Inc.|Method for joining graphite to graphite|
    US4371825A|1981-06-04|1983-02-01|Energy Development Associates, Inc.|Method of minimizing the effects of parasitic currents|
    US4534833A|1982-05-03|1985-08-13|Energy Development Associates, Inc.|Zinc-chloride battery in a chlorine producing/consuming plant|
    YU122483A|1983-06-02|1986-02-28|Aleksandar Despic|Bipolar element of a chemical current source|
    US4518664A|1983-07-01|1985-05-21|Energy Development Associates, Inc.|Comb-type bipolar stack|
    US4567120A|1984-10-01|1986-01-28|Energy Development Associates, Inc.|Flow-through porous electrodes|
    US4746585A|1986-04-07|1988-05-24|Energy Development Associates, Inc.|Comb-type bipolar stack|
    EP0428726B1|1988-08-12|1996-10-30|Koa Oil Company, Limited|Air cell|
    US20090239131A1|2007-01-16|2009-09-24|Richard Otto Winter|Electrochemical energy cell system|
    US8114541B2|2007-01-16|2012-02-14|Primus Power Corporation|Electrochemical energy generation system|
    US8273472B2|2010-02-12|2012-09-25|Primus Power Corporation|Shunt current interruption in electrochemical energy generation system|
    US8450001B2|2010-09-08|2013-05-28|Primus Power Corporation|Flow batter with radial electrolyte distribution|
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    WO2012148569A2|2011-03-01|2012-11-01|Aquion Energy Inc.|Profile responsive electrode ensemble|
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    KR101264495B1|2011-03-10|2013-05-14|로베르트 보쉬 게엠베하|Secondary Battery And Battery Pack having thereof|
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    US9130217B2|2012-04-06|2015-09-08|Primus Power Corporation|Fluidic architecture for metal-halogen flow battery|
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    CN106876152B|2015-12-11|2019-04-09|中芯国际集成电路制造有限公司|A kind of super capacitance cell and its manufacturing method|
    US10290891B2|2016-01-29|2019-05-14|Primus Power Corporation|Metal-halogen flow battery bipolar electrode assembly, system, and method|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US05/770,725|US4100332A|1977-02-22|1977-02-22|Comb type bipolar electrode elements and battery stacks thereof|
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