• 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 a method of improving the current supply of electrolysis cells such as used in the production of aluminum by igneous electrolysis of alumina dissolved in cryolite, in which the cells are aligned in a lengthwise direction, allowing the harmful influence of the induced magnetic fields to be reduced.
    公开号:SU738518A3
    申请号:SU782563048
    申请日:1978-01-12
    公开日:1980-05-30
    发明作者:Морель Поль；Дюгуа Жан-Пьер；Лангон Бернар
    申请人:Алюминиюм Пешинэ (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to the field of aluminum production, in particular, by electrolysis of molten salts in electrolyzers with longitudinal placement in the housing. Known busbar aluminum cell with two-sided supply of current to the anode bus through the drain located at the input and output ends of the cathode casing, the cathode rods of which are divided into groups connected to self-contained packages of cathode tires, in which the current to the input and output cathodes t is asymmetrical in a ratio close to 2: 1. A disadvantage of the known technical solution is a reduction in production. electrolysis cells with an increase in the unit capacity of the electrolysis cell due to the increase in current, especially in series with a nominal current above 100 kA. As the current of the cell increases, the magnetic field and electromagnetic forces in the molten aluminum increase. Uncompensated electromagnetic forces induce the circulation of the melt and, distortion of its level, which leads to a decrease in the performance of the electrolysis process. The purpose of the invention is to improve the performance of high unit capacity electrolyzers with a high degree of compensation of electromagnetic forces in the melt due to the redistribution of the magnetic field in it. To do this, packages of cathode tires of groups of rods closest to the input end of the cathode casing are connected to the stands located at the input end, and the remaining groups with cages located along the sides of the cathode casing of the subsequent electrolyzer. At the same time, if the rolling rods are divided into two groups, then the one located to the side of the board is connected to the anode bus in its middle, and when dividing the cathode rods of one side into three groups, the stoves are placed so that their connection with the anode bus. the length into sections of length 1: 3 and 2: 3, respectively. , FIG. 1 shows a diagram of the bus-bar when dividing the cathode rods of one side of the cathode casing into two groups, B, plan; in fig. 2 - the same, when divided into three groups. The electrolyzers 1 and 2 are located one after the other along the longitudinal axis of the housing, connected in a series electric circuit by a busbar containing anode tires 3, 4, stands 5, 6ji located at the input end of the cathode housing 7, b; cathode rods 9, divided into two groups 10 and 11, 12 and 13 from each side, respectively (Fig. 1), or three groups 10 and 11, 12 and 13, 14 and 15 (Fig. 2), each: and of which The cathode busbars 16, 17, 18, 19, 20, 21 are connected to the independent pack. Moreover, the bus packs 16 and 18 are connected to the stoppers 5 and 6, and the bus packs 17 and 19 to the stoppers 22, 23 located along the sides cathode housing when the cathode rods are divided into two groups. If the cathode rods are divided into three groups of 10, 11/14, and 12, 13, 15, then the packages of cathode tires 17 and 19 are connected to the sinks 24 and 25, and the packages of the tires 20 and 21 are connected to the sinks 26 and 27. The current from Stacks 24, 25 and 26, 27 are fed to anode tires 3 and 4 at points 28 and 29, which divide the length of the tires in ratios 1: 3 and 2: 3. The implementation of a current-equivalent according to the above scheme of bus-bar leads to a significant decrease in the horizontal components of the magnetic field, equalizing their values over the area of the liquid cathode. At the same time, a significant reduction in the vertical components of the floor in the corners and their differences along the sides of the cathode shell is achieved. The use of this busbar allows you to increase the current in the electrolyzer by 30%, the current efficiency to bring dg
    70 P No. 10 11/7 3; g
    权利要求:
    Claims (3)
    [1]
    yy 8% and increase productivity by 40 kg / day. Claim 1. Insertion of the stranded aluminum electrolyzers in their longitudinal arrangement in the housing, comprising anode tires, stands located at the inlet and outlet ends of the cathode housing, and cathode rods divided into groups, each of which is connected to a separate cathode tire package characterized in that, in order to increase the performance of the electrolyzer, the packages of cathode tires of groups of rods closest to the input end of the cathode housing are connected to the stands, located at the input end, and the rest The second groups of cathode rods are with sinks located along the sides of the cathode casing of the subsequent electrolyzer.
    [2]
    2. The busbar arrangement according to claim 1, wherein when dividing the cathode rods into two groups, one hundred k located at the bead is connected to the anode bus in its middle, and when dividing the cathode rods into three groups, the stoves are located so. that they are connected to the anode bus at points that divide its length, respectively, in ratios 1: 3 and 2:
    [3]
    3. Sources of information taken into account in the examination 1. USSR author's certificate 168457, cl. C 25 C 3/16, 1963.
    类似技术:
    公开号 | 公开日 | 专利标题
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    ES8200410A1|1981-10-16|Process and device for suppressing magnetic disturbances in electrolytic cells.
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    ES8203988A1|1982-04-01|Monopolar electrolytic cell of the filter press type.
    ES483012A1|1980-04-16|Electrolytic reduction cell with compensating components in its magnetic field
    JPS6096784A|1985-05-30|Electrolytic cell of electric current power more than 250000 ampere for manufacture of aluminum by hall process
    US3775281A|1973-11-27|Plant for production of aluminum by electrolysis
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    SU461662A1|1977-12-05|Method of installing busbars on aluminium electrolyzers
    RU1284273C|1995-03-27|Cathode bus arrangement of electrolyzer for producing aluminum
    RU2092622C1|1997-10-10|Device for powering consecutively connected electrolyzer cells
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    同族专利:
    公开号 | 公开日
    BR7800308A|1978-10-10|
    IS2424A7|1978-07-20|
    PL204090A1|1978-11-20|
    GR62653B|1979-05-17|
    AT363698B|1981-08-25|
    NO150364B|1984-06-25|
    PL110620B1|1980-07-31|
    OA05858A|1981-05-31|
    ES466124A1|1978-10-16|
    NO780180L|1978-07-20|
    AU3249278A|1979-07-26|
    ATA26778A|1981-01-15|
    US4132621A|1979-01-02|
    MX143708A|1981-06-25|
    CH627793A5|1982-01-29|
    DE2801650C2|1985-03-14|
    ZA78323B|1979-02-28|
    CA1100906A|1981-05-12|
    FR2378107B1|1980-03-07|
    SE422693B|1982-03-22|
    DE2801650A1|1978-07-20|
    NZ186244A|1982-03-16|
    YU39833B|1985-04-30|
    IT1092269B|1985-07-06|
    IS1468B6|1991-09-24|
    FR2378107A1|1978-08-18|
    SE7800610L|1978-07-20|
    IT7819305D0|1978-01-17|
    AU507913B2|1980-02-28|
    NO150364C|1984-10-03|
    NL7800624A|1978-07-21|
    JPS5732719B2|1982-07-13|
    GB1597933A|1981-09-16|
    JPS5391078A|1978-08-10|
    YU9378A|1982-06-30|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    RU2536577C2|2012-02-17|2014-12-27|Общество с ограниченной ответственностью "Объединенная Компания РУСАЛ Инженерно-технологический центр"|Basbar of powerful aluminium electrolyser with their lateral arrangement in housing|DE1010744B|1955-06-03|1957-06-19|Vaw Ver Aluminium Werke Ag|Rail guide for large electrolysis cells for aluminum electrolysis|
    NO122680B|1970-06-25|1971-07-26|Ardal Og Sunndal Verk|
    CH542933A|1970-09-01|1973-10-15|Alusuisse|System consisting of a series of cells for the production of aluminum by electrolysis|
    SU458616A1|1971-12-22|1975-01-30|Государственный Научно-Исследовательский Энергетический Институт Им. Г.М.Кржижановского|Scheme of aluminum electrolyzer busbars|
    SU434135A1|1973-02-16|1974-06-30|Н. П. Будкевнч, С. Э. Гефтер, И. Гнесин, А. С. Деркач, С. В. Евдокимов, Н. А. Калужский, И. Г. Киль, В. П. Никифоров,|
    JPS5216843B2|1973-10-26|1977-05-12|
    FR2324761B1|1975-09-18|1980-01-04|Pechiney Aluminium|
    FR2333060B1|1975-11-28|1980-04-30|Pechiney Aluminium|NO139525C|1977-07-14|1979-03-28|Ardal Og Sunndal Verk|DEVICE FOR COMPENSATION OF HORIZONTAL MAGNETIC FIELDS IN MELTING ELECTROLYSIS OVENS|
    FR2423554B1|1978-02-08|1981-01-16|Pechiney Aluminium|
    CH649317A5|1978-08-04|1985-05-15|Alusuisse|ELECTROLYSIS CELL WITH COMPENSATED MAGNETIC FIELD COMPONENTS.|
    DE3009158A1|1980-02-01|1981-08-06|Schweizerische Aluminium AG, 3965 Chippis|RAIL ARRANGEMENT FOR ELECTROLYSIS CELLS|
    DE3009096A1|1980-02-01|1981-08-06|Schweizerische Aluminium AG, 3965 Chippis|ASYMMETRICAL RAIL ARRANGEMENT FOR ELECTROLYSIS CELLS|
    EP0084142B1|1982-01-18|1987-06-10|ALUMINIA S.p.A.|Method and apparatus for electric current supply of pots for electrolytic production of metals, particularly aluminium|
    FR2868436B1|2004-04-02|2006-05-26|Aluminium Pechiney Soc Par Act|SERIES OF ELECTROLYSIS CELLS FOR THE PRODUCTION OF ALUMINUM COMPRISING MEANS FOR BALANCING THE MAGNETIC FIELDS AT THE END OF THE FILE|
    RU2316619C1|2006-04-18|2008-02-10|Общество с ограниченной ответственностью "Русская инжиниринговая компания"|Apparatus for compensating magnetic field induced by adjacent row of connected in series high-power aluminum cells|
    CA2877649C|2012-07-17|2016-10-18|Obshchestvo S Ogranichennoy Otvetstvennost'yu "Obedinennaya Kompaniya Rusal Inzhenerno-Tekhnologicheskiy Tsentr"|Bus bar of aluminium reduction cells of end-to-end arrangement|
    WO2018181365A1|2017-03-27|2018-10-04|三菱ケミカル株式会社|Porous membrane, membrane module, water treatment device, and method for manufacturing porous membrane|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR7702213A|FR2378107B1|1977-01-19|1977-01-19|
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