• 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 electrolytic production of aluminum by the electrolysis of cryolite-alumina melts using carbon graphite anodes. The purpose of the invention is to reduce power consumption. The steel lead of the anode 1 of the aluminum electrolysis cell 4 is made with a reduced section in the upper part 5. The upper part with a reduced section is 30% of the entire length of the rod. The area of the reduced section is equal to 60% of the cross-sectional area of the lower part. The reduced section of the upper part of the rod may be in the form of a circle or a ring. Such an embodiment of the current-carrying rod reduces heat loss through the body of the rod and allows reducing the electric power consumption by 200-300 kWh / ton of aluminum. 2 hp f-ly, 4 ill. g SU)
    公开号:SU1419522A3
    申请号:SU853900952
    申请日:1985-05-28
    公开日:1988-08-23
    发明作者:Лангон Бернар
    申请人:Алюминиюм Пешинэ (Фирма)；
    IPC主号:
    专利说明:

    293
    so you
    N3
    75J
     CM
    eleven
    The invention relates to the production of aluminum by the electrolysis of cryolithoglins of ozemic melts using carbon graphite anodes.
    The purpose of the invention is to reduce power consumption.
    FIG. 1-3 shows a steel lead for annealed anode of an aluminum electrolysis cell; in fig. And - the same for the self-burning anode.
    The carbon-graphite block of the anode 1 is made with a recess 2, With the help of a cast-iron pouring 3, a steel rod 4 is installed, made in the upper part 5 with a reduced section. The bar is attached to the anode bus 6. When using a self-burning anode



    0
    five
    localized exactly above the anode (Fig. 1). Therefore, it is sufficient to heat insulate this zone with a heat insulator, for example, alumina, in order to eliminate most of the heat losses in the zone, the middle and upper parts of the rod can be left in the air due to the relatively low temperature of 300 ° C or lower.
    An increase in the fall of the ohmic voltage in the constricted part can be compensated for by an increase in the cross section of the hot part of the steel, where high resistivity occurs. Specific temperature coefficient
    The electrical resistance of iron is 0.0147 at 500 s. This ve
    current is supplied through steel
    A rod-pin 7 is installed in a carbon-graphite paste 8. The thermal insulation is carried out with granules 9. In the baths that use pre-burnt anodes, about half of the heat flux passing through the anodes is released through the steel. Heat transfer is mainly carried out by conduction. The dotted line XX marks the boundary between the part of the conductor embedded in carbon and its upper part.
    Partial reduction of the steel cross section in the upper part allows locally to obtain high temperature gradients. As a result, hot and cold zones can be accurately determined in the steel.
    An experiment was conducted, resulting in a reduction of 10 cm in length,
    temperature reduction from 650 to 320 C (Fig. 1).
    Fig. 2 shows how the temperature distribution in the anode system occurs when the rod 4 has a constant cross section in the known anodes and under identical conditions.
    The current density can be locally increased without a melting effect. Indeed, due to the proximity of a large mass of steel with a relatively low temperature, rapid heat absorption occurs as a result of the Joule effect, with an excessive increase in current in a round rod 4.
    Increasing the temperature of the steel, which is a source of heat loss due to convection and radiation,
    0
    5 o
    five
    0
    five
    five
    The mask reaches its maximum at a temperature of about 500 ° C.
    In addition, the contact between steel and carbon is improved by increasing the cross section of the lower part of the rod 4, increasing the temperature of this zone and additional thermal expansion of the metal part. The gain in resistance of the contact thus obtained is about 30% compared with the installation of a known construction (Fig. 2).
    The cross section and length of the constricted and non-constricted parts are selected so that the resulting thermal resistance is equal to or slightly greater than the resistance of the assembly of a known construction. In this connection, it is necessary that the length of the constricted part of the upper portion 5 be the greater, the closer its section to the cross section of the original rod. This condition also requires a certain relationship between the section of the part of the upper section 5 and the section of the rod 4.
    The invention is particularly effective in the case when the ratio between the cross section of the portion of the upper portion 5 and the cross section of the rod 4 is equal to or less than 0.6. The length of the constricted part should be at least 35% of the total length of the upper part of the rod. This makes it possible to balance the total thermal resistance without manifesting a melting effect, while obtaining a gain in contact resistance that in all cases exceeds its initial value by 30%.
     Possible embodiments of the invention: the cross section of a reduced hour
    These may be PyPO.P11S110 in the form of a circle or ring (Fig. 3).
    The use of such a mounting in a known bath with a current of 280000 A made it possible to state that the coating of a rod with a larger cross section with alumina is sufficient for a very good thermal insulation of the anodes. The current density D in this case is the following: cross (cold zone) 15 A / cm, rod - narrowed zone of the upper section 5 28 A / cm, hot rod zone 4 10 A / cm.
    When comparing the operation of the electrolyzer at 280000 A with round anodes with a constant cross section of 120 mm and with the proposed anodes, it was observed that the latter provide a gain of 30 mV in the fall of the anode voltage. As a result, the energy consumption of the electrolyzer is reduced by 100 kWh / t, and the operating voltage of the electrolyzer is reduced by 0.03 V without changing the current. In this case, the total thermal resistance of the rod and its narrowed part by 50% exceeds the thermal resistance of the rod with a constant diameter of 120 mm. This provides additional thermal insulation of the electrolyzer, which allows reducing the power supplied to the electrolyzer.
    In the case of a self-burning anode (Fig. 4), the current is supplied with a help of steel rods - pins 7, which are inserted directly into the carbon-graphite paste 8, then removed and re-installed a little higher as the anode burns, but so as to avoid contact between the lower pointed the end of the pin And electrolyte. The diameter of the upper part of the pin is 100522
    150 mm, it is possible to reduce below the contact zone the pin on the anode frame and increase the diameter of the lower part. Thermal insulation of the upper part of the anode in this case is provided by granules of carbon paste 9, periodically added to restore the anode as its lower part wears out. For
    Q facilitating the extraction of the pin from the paste, it is preferable to use a construction with a pipe having the same outer diameter as the lower part of the pin.
    5 The use of the invention reduces the power consumption by 200-300 kWh / ton of aluminum and increases the service life of the cladding aluminum — steel, which becomes equal to the service life of the steel elements.
    权利要求:
    Claims (3)
    [1]
    1.Steel current lead bar 5 of the aluminum electrolysis cell for producing aluminum by electrolysis of cryolite-alumina melts, made
    from the top and bottom parts and connecting the anode busbar with carbon fiber anode, characterized in that, in order to reduce power consumption, the upper part of the rod is not less than 30% of the entire length and is made with a section of not more than 60% of the area cross section of the lower part.
    [2]
    2. The rod according to claim 1, characterized in that the upper part
    d has a cross section in the form of a circle.
    [3]
    3. Shtanga pop. 1, characterized in that the upper part has a cross section in view of the ring.
    FIG. 2
    Y07
    750
    950
    Fi9.3
    fm.4
    类似技术:
    公开号 | 公开日 | 专利标题
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    US4853941A|1989-08-01|D.C. arc furnace having electrically conductive hearth and method for making same
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    US6551473B1|2003-04-22|Electrolytic cell arrangement for production of aluminum
    US4512023A|1985-04-16|Electrodes for glass furnaces
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    SU671391A1|1991-11-23|Inventory head
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    US3107212A|1963-10-15|Method and apparatus for baking and preheating bottoms of electrolytic cells by meansof alternating or direct current
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    RU2101393C1|1998-01-10|Method of baking of electrolyzer after capital repair
    GB2098839A|1982-11-24|Electrode for arc furnace and method of producing steel
    SU546666A1|1977-02-15|Electrolyzer cathode block
    同族专利:
    公开号 | 公开日
    US4612105A|1986-09-16|
    HUT37963A|1986-03-28|
    IS3013A7|1985-11-30|
    GB2159538B|1988-01-13|
    DE3560463D1|1987-09-17|
    NO852120L|1985-12-02|
    FR2565258B1|1986-08-29|
    EP0167461A1|1986-01-08|
    HU195261B|1988-04-28|
    PL253648A1|1986-04-08|
    ES296536Y|1988-04-16|
    BR8502538A|1986-02-04|
    RO91393A|1988-03-30|
    RO91393B|1988-03-31|
    KR850008192A|1985-12-13|
    FR2565258A1|1985-12-06|
    YU88885A|1988-04-30|
    GB8513425D0|1985-07-03|
    AU564143B2|1987-07-30|
    OA08025A|1987-01-31|
    EP0167461B1|1987-08-12|
    TR22577A|1987-02-02|
    GR851303B|1985-11-25|
    CN85104086A|1986-11-26|
    PL143780B1|1988-03-31|
    AU4304085A|1985-12-05|
    PH20844A|1987-05-08|
    GB2159538A|1985-12-04|
    JPS60258490A|1985-12-20|
    ES296536U|1987-10-16|
    ZA854050B|1986-01-29|
    AT28904T|1987-08-15|
    IS1291B6|1987-07-07|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3236753A|1961-03-21|1966-02-22|Aluminium Lab Ltd|Prebake anodes for electrolytic production of aluminum and coating therefor|
    DE1251962B|1963-11-21|1967-10-12|The British Aluminium Company Limited, London|Cathode for an electrolytic cell for the production of aluminum and process for the production of the same|
    FR1536838A|1967-09-15|1968-08-16|Huta Aluminium|Anode stud in electrolytic cells in aluminum fabrication|
    AU543106B2|1980-05-23|1985-04-04|Swiss Aluminium Ltd.|Cathod for aluminium production|
    US4526669A|1982-06-03|1985-07-02|Great Lakes Carbon Corporation|Cathodic component for aluminum reduction cell|NO162083C|1986-06-06|1989-11-01|Norsk Hydro As|ANODE HANGERS FOR CARBON-CONTAINING ANODE IN CELLS FOR PRODUCING ALUMINUM.|
    US5380416A|1993-12-02|1995-01-10|Reynolds Metals Company|Aluminum reduction cell carbon anode power connector|
    US5538607A|1995-04-12|1996-07-23|Pate; Ray H.|Anode assembly comprising an anode bar for the production of molten metal by electrolysis|
    AUPQ218899A0|1999-08-13|1999-09-02|Jakovac, Vjekoslav|Anode assembly comprising separation of electrical and mechanical functions of the assembly|
    NO315090B1|2000-11-27|2003-07-07|Servico As|Devices for conveying current to or from the electrodes in electrolytic cells, methods of making them, and electrolytic cell preparation of aluminum by electrolysis of alumina dissolved in a molten electrolyte|
    AU2004200431B8|2003-02-25|2009-03-12|Alcoa Usa Corp.|Protecting an inert anode from thermal shock|
    US7118666B2|2001-08-27|2006-10-10|Alcoa Inc.|Protecting an inert anode from thermal shock|
    EP2006419A1|2007-06-22|2008-12-24|Sgl Carbon Ag|Reduced voltage drop anode assembly for aluminium electrolysis cell|
    WO2012100340A1|2011-01-28|2012-08-02|UNIVERSITé LAVAL|Anode and connector for a hall-heroult industrial cell|
    CN102108525B|2011-04-11|2012-07-25|商丘市鑫科节能技术服务有限公司|Method for connecting electrolytic aluminum anode without pouring|
    RU2485216C1|2012-02-21|2013-06-20|Федеральное государственное автономное образовательное учреждение высшего профессионального образования "Национальный исследовательский технологический университет "МИСиС"|Electrolysis unit for aluminium manufacture|
    RU2509831C1|2012-12-11|2014-03-20|Общество с ограниченной ответственностью "Объединенная Компания РУСАЛ Инженерно-технологический центр"|Aluminium electrolytic cell anode holder|
    RU2535438C1|2013-06-24|2014-12-10|Общество с ограниченной ответственностью "Объединенная Компания РУСАЛ Инженерно-технологический центр"|Anode holder bracket|
    FR3016897B1|2014-01-27|2017-08-04|Rio Tinto Alcan Int Ltd|ANODIC ASSEMBLY AND METHOD OF MANUFACTURING THE SAME.|
    CN106471160B|2014-07-04|2018-10-16|力拓艾尔坎国际有限公司|Anode assemblies|
    WO2016039978A1|2014-09-08|2016-03-17|Alcoa Inc.|Anode apparatus|
    CN105543895B|2016-02-26|2018-08-14|周俊和|A kind of mechanical anode steel claw structure of pre-calcining electrolytic cell|
    CN110257860B|2019-07-25|2020-09-25|山西双宇新能源有限公司|Composite-formed anode conducting device and manufacturing method thereof|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR8408816A|FR2565258B1|1984-05-29|1984-05-29|PARTIALLY SHRINKED CARBON ANODE FOR TANKS FOR THE PRODUCTION OF ALUMINUM BY ELECTROLYSIS|
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