• 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:
    The invention relates to the field of non-ferrous metallurgy, to the electrolytic production of aluminum, in particular, to the construction of an electrolyzer for the production of aluminum. The purpose of the invention is to simplify the design and maintenance of the electrolyzer. A bath for producing aluminum from aluminum oxide contains an anode 1, a cathode-polarized bottom 2, a screen 3 of a layer of shaped elements 4, and means 5 for holding a screen 3 under the anode 1. Elements 4 are made of porous titanium diboride with a dense coating or of graphite coated from titanium diboride. The average density of the elements 4 is 2.1-2, x10 kg / m, i.e. less than the density of aluminum at 960 ° C, but greater than the density of the electrolyte, so the screen 3 floats at the aluminum-electrolyte interface. The distance between the screen 3 and the anode 1 is preferably 20 mm. The elements 4 of the screen 3 are mounted close to each other or are articulated to each other. In electrolysis, they are a cathode, they can freely move relative to each other under the action of a metal wave. The change of elements 4 can be carried out without dismantling the electrolyzer. 1 hp f-ly. 3 il. CO DO SP O5 with O5
    公开号:SU1356967A3
    申请号:SU833610550
    申请日:1983-06-27
    公开日:1987-11-30
    发明作者:Леруа Мишель；Кейнборг Морис
    申请人:Алюминиюм Пешинэ (Фирма)；
    IPC主号:
    专利说明:

    / 7 / /// /// /// /// /// /// 7/ /// ///
    ut.J
     2
    one
    The invention relates to non-ferrous metallurgy, to the electrolytic production of aluminum, in particular to the construction of an electrolyzer for the production of aluminum,
    The aim of the invention is to simplify the design and maintenance of the electrolyzer.


    FIG. 1 shows the electrolysis IQ of the process of electrolysis on the surface
    aluminum bath, general appearance; in fig. 2 - screen; in fig. 3 - a node connecting the shaped elements together.
    The electrolysis bath for the production of aluminum from alumina contains an anode 1, a cathodically polarized bottom 2 baths, a screen 3 of a layer of shaped elements 4, and means 5 for holding a screen 3 under the anode 1. The shaped elements 4 can be made in the form of balls of porous titanium diboride with a dense coating, or of graphite with a coating of titanium diboride. Here, the average density of the material of the elements 4 is 2.1-2.310 kg / m (Fig. 1).
    Another embodiment of the elements 4 are graphite tiles coated with titanium diboride to give them an average density of 2.1-2.310 kg / m (Fig. 2). These tiles, as well as the balls, are located close to each other and are not interconnected.
    To prevent the electrical contact of the tiles with the anode 1 on: they are made of protrusions -6 of non-conductive material, for example, boron nitride, aluminum or red carbide.
    Elements 4 in the form of tiles can be pivotally interconnected (Fig. 3). The distance between the anode 1 and the screen 3 is less than 40 mm, preferably 20 mm.
    Electrolysis bath works as follows.
    In the process of electrolysis on the cathode polarized bottom 2, liquid aluminum is separated and collected in a further layer of liquid aluminum serves as a cathode.
    Screen 3 floats at the aluminum-electrolyte interface, since the density of the shaped elements 4 is less than the density of aluminum (2.310 kg / m, but greater than the density of the electrolyte (2.1-2.2-10 kg / m) at the electrolysis temperature (960 C) .
    The surface of the elements 4 is made of titanium diboride, i.e. material well wetted by liquid aluminum. Therefore, the aluminum released in the proelements 4, which are cathodically polarized and serve as the cathode, does not enter the electrolyte in the form of droplets (remains in the form of a layer on the elements 4 and flows into the underlying aluminum layer).
    This makes it possible to reduce the interelectrode distance to less than 40 mm, preferably up to 20 mm, without the risk of the aluminum trapping the anode. Reducing the distance between the anode 1 and the screen 3 reduces the power consumption for producing aluminum. Making the screen 3 of unrelated elements 4 (or pivotally interconnected) simplifies the construction of the bath and its maintenance, so that the elements 4 can be easily replaced without stopping and dismounting the bath.
    权利要求:
    Claims (2)
    [1]
    1. An electrolysis bath for the production of aluminum from alumina in a cryolite melt containing at least one anode, a cathode-polarized bottom, a screen made up of a layer of shaped elements made of a material resistant to the action of molten aluminum and electrolyte,
    with good electrical conductivity and density of 2.1-2.3 -10 kg / m, and means for holding the screen under the anode, characterized in that, in order to simplify the design and maintenance of J, the shaped elements are made of porous titanium diboride with a dense coating or of graphite coated with titanium diboride, located close to each other or connected to each other hingedly.
    [2]
    2. The bath of claim 1, wherein the distance between the gc anode and the screen is less than 40 mm, preferably 20 mm.
    Ft
    If 6j-Ai /
    h t 1
    FIG. 2
    j-Ai /
    h t 1
    Phie. J
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    同族专利:
    公开号 | 公开日
    ZA834761B|1984-03-28|
    FR2529580B1|1986-03-21|
    US4533452A|1985-08-06|
    DE3365289D1|1986-09-18|
    GR77515B|1984-09-24|
    OA07473A|1984-12-31|
    CA1190892A|1985-07-23|
    FR2529580A1|1984-01-06|
    AU562447B2|1987-06-11|
    IN159794B|1987-06-06|
    KR840006510A|1984-11-30|
    YU140683A|1985-12-31|
    NO832365L|1984-01-02|
    EP0099840A1|1984-02-01|
    ES8403984A1|1984-04-01|
    ES523678A0|1984-04-01|
    JPS6141997B2|1986-09-18|
    EP0099840B1|1986-08-13|
    AU1646083A|1984-01-05|
    BR8303459A|1984-02-07|
    JPS5920484A|1984-02-02|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    BE433408A|1938-04-08|
    US3287247A|1962-07-24|1966-11-22|Reynolds Metals Co|Electrolytic cell for the production of aluminum|
    GB1169012A|1965-10-21|1969-10-29|Montedison Spa|Furnace and Process for Producing, in Fused Bath, Metals from their Oxides, and Electrolytic Furnaces having Multiple Cells formed by Horizontal Bipolar Carbon Electrodes|
    US4338177A|1978-09-22|1982-07-06|Metallurgical, Inc.|Electrolytic cell for the production of aluminum|
    US4177128A|1978-12-20|1979-12-04|Ppg Industries, Inc.|Cathode element for use in aluminum reduction cell|
    US4224128A|1979-08-17|1980-09-23|Ppg Industries, Inc.|Cathode assembly for electrolytic aluminum reduction cell|
    GB2069530B|1980-01-28|1984-05-16|Diamond Shamrock Corp|Packed cathode bed for electrowinning metals from fused salts|
    CH644406A5|1980-04-03|1984-07-31|Alusuisse|MELT FLOW ELECTROLYSIS CELL FOR THE PRODUCTION OF ALUMINUM.|
    US4349427A|1980-06-23|1982-09-14|Kaiser Aluminum & Chemical Corporation|Aluminum reduction cell electrode|
    ZA824255B|1981-06-25|1983-05-25|Alcan Int Ltd|Electrolytic reduction cells|
    CH648870A5|1981-10-23|1985-04-15|Alusuisse|CATHOD FOR A MELTFLOW ELECTROLYSIS CELL FOR PRODUCING ALUMINUM.|
    FR2518124B1|1981-12-11|1984-02-17|Pechiney Aluminium|
    US4436598A|1983-09-28|1984-03-13|Reynolds Metals Company|Alumina reduction cell|EP0145411B1|1983-11-29|1988-01-27|Alcan International Limited|Aluminium reduction cells|
    US4631121A|1986-02-06|1986-12-23|Reynolds Metals Company|Alumina reduction cell|
    US4919782A|1989-02-21|1990-04-24|Reynolds Metals Company|Alumina reduction cell|
    US5129998A|1991-05-20|1992-07-14|Reynolds Metals Company|Refractory hard metal shapes for aluminum production|
    EP0572896B1|1992-05-25|1998-01-07|Canon Kabushiki Kaisha|Magnetic developer and recognition method of magnetic-ink character|
    US5486278A|1993-06-02|1996-01-23|Moltech Invent S.A.|Treating prebaked carbon components for aluminum production, the treated components thereof, and the components use in an electrolytic cell|
    US5472578A|1994-09-16|1995-12-05|Moltech Invent S.A.|Aluminium production cell and assembly|
    US5753382A|1996-01-10|1998-05-19|Moltech Invent S.A.|Carbon bodies resistant to deterioration by oxidizing gases|
    WO2018092103A1|2016-11-19|2018-05-24|Jan Petrus Human|Electrodes for use in the electro-extraction of metals|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR8211873A|FR2529580B1|1982-06-30|1982-06-30|ELECTROLYSIS TANK FOR THE PRODUCTION OF ALUMINUM, COMPRISING A FLOATING CONDUCTIVE SCREEN|
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