• 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:
    1433075 Electrode compositions SWISS ALUMINIUM Ltd 15 May 1974 [25 May 1973] 21590/74 Headings C1J and C1A [Also in Division C7] A ceramic oxide, useful in the electrolysis of a melt, e.g. based on cryolite or alumina for Al production, is based on SnO 2 , Fe 2 O 3 , Fe 3 O 4 , Cr 2 O 3 , Co 3 O 4 , NiO or ZnO with optional doping amounts of other metal oxide(s) to increase conductivity ; e.g. SnO 2 containing 0À01-20% by wt. of at least one of Fe 2 O 3 , Sb 2 O 3 , CuO, MuO 2 , Nb 2 O 5 , ZnO, Cr 2 O 3 , Co 3 O 4 or WO 3 . The ceramic oxide may surround a conductive core which acts as power connection/current distributor, e.g. of Ni, Cu, Co, Mo, Ag or a conductive boride, carbide or nitride. The oxide is made by isostatic compression of a blend of its component oxides, followed by high temperature sintering of. the green product.
    公开号:SU708999A3
    申请号:SU742043450
    申请日:1974-05-24
    公开日:1980-01-05
    发明作者:Альдер Ханспетер
    申请人:Швейцерише Алюминиум Аг (Фирма)；
    IPC主号:
    专利说明:

    I
    The invention relates to the field of metallurgy of non-ferrous metals, in particular to the production of aluminum by the electrolysis of molten salts.
    The anode of the electrolyzer is known for producing aluminum from molten electrolytes, the working surfaces of which are made of an oxyceramic material. The oxide ceramics contains 80-99%.
    The disadvantage of the anode lies in its considerable corrosion and contamination by the aluminum material of the anode. This is due to the interaction of SnOj with aluminum, which is in suspension in the electrolyte. Corrosion is particularly pronounced in the three-phase zone between the anode, the electrolyte and the gas atmosphere.
    The purpose of the invention is to increase the service life of the anode and the durability of the corrosive environment.
    This goal is achieved by the fact that a part of the anode located in the three-phase zone is covered with a protective layer of non-conducting and melt-resistant electrolyte material selected from the group containing sintered alumina and magnesia.
    hardened electrolyte and refractory nitrides.
    As basic materials, the dp of manufacture, anode, is dissolved, Fe ,, Ox, CrO, COjOx., NiO or ZnO, mainly 80-99.7% SnO. Tin oxide has the following advantages: insignificant sensitivity to thermal shock; solubility in cryolite is very low (0.08% at 1000 ° C). To improve sintering, density and conductivity of SnO2, additives from oxides of the following metals are used individually or in combination:
    s
    Fe Cu Mn Nb Zn COy Cr W, Sb,
    Cd, Zr, Ta, Ni, Ca, Ba, Bi, 3n. .
    The anode of SnO2.f immersed in the molten cryolite without a current load, interacts with the aluminum, which is in suspension in the cryolite, by the reaction:
    ЗЗпО 2 + 4А1 +.
    At the anode under load, wear occurs significantly
    5 faster, especially in the three-phase zone, i.e., the region of transition from the electrolyte to the gas atmosphere of the electrolyzer,
    权利要求:
    Claims (1)
    [1]
    In order to reduce the corrosion of the anode, it is necessary to apply a protective ring of current and melt-resistant electrolyte to the surface of the anode in a 1-phase zone. This colo can be obtained in two types: the side surfaces of the anode are shielded in part by coating of sintered alumina, magnesia or of refractory nitrides, for example nitri. Yes boron crust formation from frozen electrolyte due to local cooling of the anode. The drawings show various versions of the anodes, according to the invention and electrolyzers equipped with them. FIG. 1 shows the ceramic anode ic with the fully shielded side surface of FIG. electrolyte side surface; in fig. 3 - anode with side walls completely shielded with POM1TSI peel; in Fig. 4, the anode is completely immersed in an electrolyte with a shielded current lead; on. Fig. 5 shows a horizontal anode plate with OXIDE-oxidized anode blocks MADE UP separately; FIGS. b are sections of FIG. 5; Fig. 7 shows a cell with a horizontal anode; Fig, 8 elvktroliz. p with multiple anodes; Fig. 9 shows a cell with a certain number of alternately arranged anodes and cathodes. The anode 1 consists mainly of doped tin oxide and is at least partially in contact with the electrolyte. The current lead 2 is made of metal or another conductive material such as nitride carbide or boride. The protective layer 3 of the anode 1 is made of a poorly conducting material and f is stable with respect to the electrolyte melt. In Fig. 3, the backing layer 3 of the cylindrical anode 1 is in the form of a ring of 2, or MgD, which is previously cemented or sprayed. The protective layer 3 completely covers the lateral surface of the anode 1, which is permanently immersed in the electrolyte melt, however, it is not obligatory that the protective layer 3 covers the entire lateral surface of the anode 1. But it must shield the anode in the three-phase zone. FIG. 2 protective layer 3 to the patterns of solidified electropite And this layer with favorable yc.no can achieve a sufficient thickness. The formation of a crust of electrolyte can be facilitated by the supply of a cooling agent through channel 4 to the current supply 2, the built-in current distributor 5 reduces the internal resistance of the anode 1 and helps more evenly / Iy distribute the current on the outer surface of the anode. from congestion electrolyte. The channel 4 for supplying the cooling agent is shaped so that the side walls of the current distributor 5 can also be cooled, the Anode 1 being in contact with the electrolyte over its entire bottom surface. FIG. 4, the anode 1 is completely loaded into the electrolyte melt. Tokopeed 2 and the top surface of the anode,. covered with protective layer 3; Fig. 5 and b shows a horizontal anode plate. Separate anodes 1 of OKHCHOKepaivsiMBCKoro material are laid in the plate and are in contact with the plate of the current distributor 5 "Uniformly distributed channels b in the plate allow for the removal of anode gas with a horizontal anode 1 with channels 6 and 7 for exhaust anode gas and supply, the side surface of the anode 1 and the current lead are covered with a curved layer 3f which prevents corrosion at the three phase boundary. In order to eliminate corrosion, in the channels 6 and 7 in the lower part are provided inserts 8 and 9 of the same material, h then a protective ring. A layer of liquid aluminum 10 is assembled at the cathode 11 made of carbon, graphite or of electrically conductive melt-resistant carbide, nitride or boride. The cathode is equipped with a current lead; .-; 12, the electrolyzer is closed with a grinder 13 ". Fig. 8 shows an electrolyzer with several anodes. The designations are the same as in FIG. 1-7, the Pla of FIG. 9 shows an electrolyzer with; an number of anodes 1 and cathodes 11 alternately arranged; Current leads 2 and 12 in the region of the border of the three phases are shielded by protective layers 3; the same as in fig. 1-8. Claims of the Invention Anode of an electrolyzer for producing aluminum from molten electrolytes, whose working surfaces are made of an oxyceramic material,., Characterized in that, in order to increase the service life. and resistance to aggressive environment, a part of the anode located in the three-phase zone is covered with a protective layer of non-conductive and melt-resistant electrolyte material selected from the group consisting of sintered alumina, magnesia, solidified electrolyte and refractory nitrides. Sources of information taken into consideration at examination 1, Swiss Patent W 520779, class, C 22 d 3/02, 1972 ,,
    Puz.i
    FIG. 2
    FIG. 3
    Fig.-ff
    ; 2
    A-A.
    FIG. 6
    e //
    - //
    类似技术:
    公开号 | 公开日 | 专利标题
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    同族专利:
    公开号 | 公开日
    ES426657A1|1977-01-01|
    BR7404276D0|1975-09-30|
    PH12130A|1978-11-07|
    NO138956C|1978-12-13|
    AT331054B|1976-08-10|
    ZA743058B|1975-05-28|
    IT1012800B|1977-03-10|
    US3960678A|1976-06-01|
    FR2230750A1|1974-12-20|
    IN142822B|1977-08-27|
    NO138956B|1978-09-04|
    SE410110B|1979-09-24|
    AR204922A1|1976-03-19|
    GB1433075A|1976-04-22|
    CH575014A5|1976-04-30|
    DE2425136C2|1983-01-13|
    JPS5244729B2|1977-11-10|
    JPS5043008A|1975-04-18|
    EG11429A|1977-09-30|
    NL159728B|1979-03-15|
    BE815484A|1974-09-16|
    IS2213A7|1974-11-26|
    TR17713A|1975-07-23|
    ATA430974A|1975-10-15|
    NO741881L|1974-11-26|
    AU6928874A|1975-11-27|
    YU141974A|1982-06-30|
    OA04758A|1980-08-30|
    FR2230750B1|1978-06-02|
    IS1029B6|1980-04-14|
    NL7407007A|1974-11-27|
    CA1089403A|1980-11-11|
    DE2425136A1|1974-12-12|
    DD112288A5|1975-04-05|
    PL88790B1|1976-09-30|
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    US7685843B2|2004-07-23|2010-03-30|Saint-Gobain Ceramics & Plastics, Inc.|Tin oxide material with improved electrical properties for glass melting|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    CH752273A|CH575014A5|1973-05-25|1973-05-25|
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