• 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:

    公开号:SU1205779A3
    申请号:SU823520360
    申请日:1982-12-09
    公开日:1986-01-15
    发明作者:Кейнборг Морис；Варен Филипп；Берто Ив；Леруа Мишель
    申请人:Алюминиум Пешинэ (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to non-ferrous metallurgy, in particular to the electrolytic production of aluminum, and relates to the structural elements of the electrolyzer.
    The distance of the invention is the simplification of the cell electrolysis.
    Figures 1 and 2 depict an electrolytic cell for producing aluminum with a cathodic removable element, general view, embodiments; on fig.Z - cathode removable element, a general view; 4 and 5 show the active element of the removable element according to FIG. 3, embodiments of the embodiment; 6 to 12, a cathode removable element, embodiments. I
    The cathode removal element 1 is installed on the bottom 2 of the electrolyzer directly under the anode 3. The bottom 2 is made of a non-conductive material. The current lead to the element 1 is carried out by bus 4 with a collector through an aluminum layer.
    The cathode removable element 1 contains active elements 5 of a heat-resistant conductive material, such as titanium diboride, and an intermediate support 6, such as graphite. The average density of the removable element 1 should be less than the density of aluminum at 930–960 ° C, i.e. less than 2.3-1 O kg / m.
    The active elements 5 can be made in the form of a head 7 and a shank 8. The shanks 8 are located in the holes of the support 6. The heads 7 lie directly on the support 6 or can
    An electrolyzer for producing aluminum using the proposes to be equipped with 9 (FIG. 4 or SF10 flaps 5), which provide the 0th cathode removable element, the presence of a gap between the support 6 and the head, works as follows. hearth 2 electrolyzer.
    The potential of the anodes 3 and the cathode elements I is fed through tires 4. When current flows through the electrolyzer, aluminum is released on the active elements 5, which flows down onto the bottom 2 of the electrolyzer.
    45
    The potential of the anodes 3 and the cathode elements I is fed through tires 4. When current flows through the electrolyzer, aluminum is released on the active elements 5, which flows down onto the bottom 2 of the electrolyzer.
    During the electrolysis process, the cathode Intermediate support 6 can be filled with a groove 11 (Fig. 6) equipped with limiters. The movement of the intermediate support 6 is limited to the T-shaped support 12 on which it is installed. In this case, the target removable element is arranged in accordance with the implementation of the active elements, near the metal-to-metal interface 5 in the form of sections of cut-through pipes mounted on T-shaped projections 13 of the intermediate support 6.
    The course of movement of the cathode removable 55 element 1 defined by the height of the T-shaped support 12 must be at least equal to the varied height
    electrolyte, preventing the occurrence of waves at the metal electrolyte interface.
    Without delaying on the surface of the active elements, the sludge formed during the electrolysis process is lowered onto the bottom 2 of the electrolyzer.
    mirrors of liquid aluminum during the Electrolysis and metal fusions. In this case, the active elements 5 of titanium diboride should be above the aluminum-electrolyte interface not less than 10 mm, and the support 6 should always be immersed in aluminum.
    According to the embodiment shown in FIG. 7, the support 6 of graphite is made in the form of an I-beam, and the active element 5 is in the form of a coating of titanium diboride. The movement of the support 6 is limited to perforated concrete block 14, installed on the bottom 2 of the electrolyzer.
    According to the embodiment shown in FIGS. 9-12, the active element 5 of titanium diboride is mounted on support 6 in the form of a float. Move
    the support 6. is limited to the shoulders 15 of the support 16. The active element 5 is complete in section T and can be inserted into the holes of the support 6 in the form of a ring (Fig. 9) or into the cavity 17
    support 6, made in the form of a cuvette (Figures 11 and 12}. The cavity 17 is filled with liquid aluminum during electrolysis.
    Active Element 5 can be
    made in the form of a plate (Fig, 10) and mounted on a support 6, for example, a screw 18.
    In all cases, the density of the cathode removable element must be
    below 2.3, preferably (2.1-2, kg / m, or below
    2.1 10 kg / m at 930-960 ° C. I. ,,
    An electrolyzer for producing aluminum using the proposed cathodic removable element operates as follows. My cathodic removable element works as follows.
    A potential difference is applied to the anodes 3 and the cathode elements I via tires 4. When current flows through the electrolyzer, aluminum is released on the active elements 5, which flows onto the bottom 2 of the electrolyzer.
    In the process of electrolysis, the cathode removable element is located near the metal -
    The removable element is located near the metal -
    electrolyte, preventing the occurrence of waves at the metal – electrolyte interface.
    Without delaying on the surface of the active elements, the sludge formed during the electrolysis process is lowered onto the bottom 2 of the electrolyzer.
    The resulting metal is periodically removed from the cell.
    The use of the invention simplifies the maintenance of the electrolyzer. The hooks as separate elements are easy.
    1205779
    are replaced, and their floating nature makes them less vulnerable to mechanical shocks that can occur during operation 5.
    2
    FIG. 2
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    VNIIPI Order 8551/62 TijpaK 615 Subscription
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    Branch PPP Patent, Uzhgorod, Proektna St., 4
    权利要求:
    Claims (4)
    [1]
    1. CATHODE REMOVABLE CELL FOR ELECTROLYTIC PRODUCTION OF ALUMINUM in a cryolite melt containing an active element from heat-. a strong conductive material, such as titanium diboride, and an intermediate inert to the melt complete as a whole, which is so that, in order to simplify the maintenance of the cell, the density of the cathode element is lower than 2.3 · 10 kg / m 3, at 930960 C and the cathode element is equipped with fastening means made in the form of supports and stops of non-refractory ceramic material or metal.
    [2]
    2. The element according to π.I, characterized in that the density of the cathode element is (2,12,3) · 10 ^ kg / m 3 at 930-960 ° C.
    [3]
    3. The element according to claim 1, wherein the density of the cathode element is below 2.1 · 10 3 'kg / m 3 at. 930-960 ° C.
    [4]
    4. The cell according to claims 1 to 3, characterized in that the group of active cells is mounted on flax aluminum and electrolyte
    SU .., 1205779 figure 1
    类似技术:
    公开号 | 公开日 | 专利标题
    SU1205779A3|1986-01-15|Removable cathode element for electrolytic production of aluminium
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    US4495037A|1985-01-22|Method for electrolytically obtaining magnesium metal
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    RU2716726C1|2020-03-16|Method of applying protective coating on electrolytic cell cathodes for aluminum production
    US3389063A|1968-06-18|Process for electrolytic recovery and refining of metals
    同族专利:
    公开号 | 公开日
    CA1195950A|1985-10-29|
    NO157508C|1988-03-30|
    FR2518124B1|1984-02-17|
    EP0082096B1|1985-08-21|
    NZ202697A|1986-02-21|
    JPS58107491A|1983-06-27|
    US4532017A|1985-07-30|
    ES8402365A1|1984-01-16|
    FR2518124A1|1983-06-17|
    NO824167L|1983-06-13|
    DE3265665D1|1985-09-26|
    AU9145982A|1983-06-16|
    EP0082096A1|1983-06-22|
    AU552985B2|1986-06-26|
    OA07274A|1984-04-30|
    ES517933A0|1984-01-16|
    GR77281B|1984-09-11|
    HU191107B|1987-01-28|
    ZA829064B|1983-09-28|
    IN158855B|1987-02-07|
    PL239350A1|1983-06-20|
    JPS6127474B2|1986-06-25|
    YU268982A|1985-03-20|
    BR8207190A|1983-10-11|
    PL134338B1|1985-08-31|
    NO157508B|1987-12-21|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    RU2454490C1|2010-11-02|2012-06-27|Общество с ограниченной ответственностью "Легкие металлы"|Electrolysis unit for aluminium manufacture|US3407132A|1965-06-16|1968-10-22|Minnesota Mining & Mfg|Floating anode|
    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|
    NO764014L|1975-12-31|1977-07-01|Aluminum Co Of America|
    CH635132A5|1978-07-04|1983-03-15|Alusuisse|CATHOD FOR A MELTFLOW ELECTROLYSIS OVEN.|
    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|
    US4349427A|1980-06-23|1982-09-14|Kaiser Aluminum & Chemical Corporation|Aluminum reduction cell electrode|
    CH648870A5|1981-10-23|1985-04-15|Alusuisse|CATHOD FOR A MELTFLOW ELECTROLYSIS CELL FOR PRODUCING ALUMINUM.|US4526669A|1982-06-03|1985-07-02|Great Lakes Carbon Corporation|Cathodic component for aluminum reduction cell|
    FR2529580B1|1982-06-30|1986-03-21|Pechiney Aluminium|ELECTROLYSIS TANK FOR THE PRODUCTION OF ALUMINUM, COMPRISING A FLOATING CONDUCTIVE SCREEN|
    CH651855A5|1982-07-09|1985-10-15|Alusuisse|SOLID CATHODE IN A MELTFLOW ELECTROLYSIS CELL.|
    CH654335A5|1983-03-11|1986-02-14|Alusuisse|CELL FOR REFINING ALUMINUM.|
    AU2713684A|1983-04-26|1984-11-01|Aluminium Company Of America|Electrolytic cell|
    US4664760A|1983-04-26|1987-05-12|Aluminum Company Of America|Electrolytic cell and method of electrolysis using supported electrodes|
    US4596637A|1983-04-26|1986-06-24|Aluminum Company Of America|Apparatus and method for electrolysis and float|
    US4622111A|1983-04-26|1986-11-11|Aluminum Company Of America|Apparatus and method for electrolysis and inclined electrodes|
    US4808304A|1983-10-19|1989-02-28|Deal Troy M|Apparatus for the dewatering of phosphate slimes|
    US4631121A|1986-02-06|1986-12-23|Reynolds Metals Company|Alumina reduction cell|
    JPH0628943Y2|1988-08-10|1994-08-03|多摩川精機株式会社|Needle swing mechanism in winding machine|
    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|
    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|
    US6071388A|1998-05-29|2000-06-06|International Business Machines Corporation|Electroplating workpiece fixture having liquid gap spacer|
    GB2371055A|2001-01-15|2002-07-17|Innovation And Technology Alum|Anode for electrolysis of aluminium|
    DE102011111331A1|2011-08-23|2013-02-28|Esk Ceramics Gmbh & Co. Kg|Titanium diboride granules as erosion protection for cathodes|
    AU2014334447A1|2013-10-07|2016-05-19|Electro-Kinetic Solutions Inc.|Method and apparatus for treating tailings using an AC voltage with a DC offset|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR8123780A|FR2518124B1|1981-12-11|1981-12-11|
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