![]() Cathodic screen of electrolysis baths
专利摘要:
This invention relates to the construction of a cathode screen of electrolysis baths for the production of aluminum. The subcathode screen is made in the form of a steel sheet with a thickness of 8–12 mm with deforming zones 2–5 mm thick located in a plane located under the cathode blocks or outside this plane. The deforming zone is made of a closed or open profile with a wall thickness that is half the thickness of the steel sheet or in the form of steel sheets with relative elongation at more than 2% with a thickness that is half the thickness of the steel sheet connected to the steel sheet with a solid weld. The screen can be provided with an additional protective agent made of thin steel sheets with a thickness of less than 5 mm superimposed one on another and located between the base of the cathode blocks and the main steel sheet or connected to each cathode rod of the weld and electrically in contact with more than 50% of the surface the lower base of the corresponding cathode block, 5C. f-ly, 3 ill. CO 00 SP dream 公开号:SU1287757A3 申请号:SU843737945 申请日:1984-05-15 公开日:1987-01-30 发明作者:Берто Ив;Леруа Мишель 申请人:Алюминиюм Пешинэ (Фирма); IPC主号:
专利说明:
1,128 The invention relates to the electrolytic production of aluminum, to the structural elements of electrolysis cells, in particular to the subcathode screen of electrolysis vines for the production of aluminum by the method of Ha11-Neutlt. Fig, 1 shows a cell with a cathode screen, a cross-section; in Fig.2 and 3 - electrolysis Vakna with other subcathode screens; Figures 4 and 5 are a sub-cathode screen with different deforming zones. The subcathode screen of the electrolysis baths for the production of aluminum is made in the form of steel sheet 1 with a thickness of 8-12 mm with deforming zones 2. The steel sheet 1 is placed in the liner 3 of the bath 4 under the base of the cathode blocks 5 with cathode cores 6. The bath 4 is enclosed in a metal casing 7. On top of the electrolyte filling the bath 4, the anodes are lowered 8 The deforming zone 2 is located under the cathode blocks 5 (Fig.2, 3) or outside (Fig.1). If the deforming zones 2 are located outside the cathode blocks 5 (Fig. O, they are made in the form of steel sheets 2-5 mm thick (half the thickness of sheet 1) with relative elongation at 20 ° C more than 2% and welded to sheet 1 solid welded shchivom 9. The deforming zone 2 can also be made in the form of a closed circular profile (Fig. 2, 3) or square (Fig. 4) section. In this case, the profile wall thickness is half the thickness of the steel sheet 1. The profile in the form of which the deforming zone 2 is made can also be made open (Figures 4, 5). The efficiency and durability of the sub-cathode screen can be increased due to additional protective equipment made in the form of a set of thin steel sheets 10 with a thickness of less than 5 mm and located between the base of the cathode blocks and the main steel sheet 1 (Fig. 2); Additional protective agent may be made in the form of steel sheets 11 connected to each a cathode rod 6 by a weld and electrically contacting with more than 50% of the surface of the lower base of the corresponding cathode block 5 (FIG. 3). An electrolyzer for producing aluminum using the proposed subcathode screen works as follows. The electrolysis bath 4 is filled with electrolyte, a potential difference is applied to the cathode blocks 5 and the anodes 8. When current flows through the electrolyte, aluminum is released on the cathode blocks. A subcathode screen located in the liner 3 of the bath 4 prevents the flow of electrolyte and aluminum further into the liner 3. The presence of deforming zones 2 makes it possible to compensate for the difference in temperature expansions of the central and peripheral parts of the screen, caused by the difference in temperature directly under the cathode blocks 5 and at the periphery of the bath 4. This increases the service life of the electrolyzer. The location of the deforming zone 2 outside of the cathode blocks 5, and its execution in the form of a thin steel sheet makes it possible to reduce heat losses. I An additional protective agent in the form of a set of thin steel sheets 10 prevents the penetration of sodium and fluorine, especially during the first months of operation of the electrolysis bath 4. The additional protective agent in the form of steel sheets 11 is the first obstacle to the penetration of metal and electrolyte, does not form an electrochemical cell. sheet 1, i.e. electrochemical corrosion is prevented.
权利要求:
Claims (6) [1] 1. Subcathode screen of electrolysis baths to prevent melt from penetrating into the refractory and insulating lining to produce aluminum, comprising a steel sheet located in the refractory insulating lining of the bath under the base of the cathode carbon blocks with cathode rods with overlapping of the entire subcathode space characterized by. that, with the goal of increasing the service life of the electrolyzer and reducing the tag losses through the bottom, the steel sheet is 8–12 mm thick with deforming zones 2–5 mm thick located in a plane located under the cathode blocks or outside the plane under the cathode blocks in blocks. [2] 2. The screen according to claim 1, characterized in that the deforming zone is made of a closed profile with a wall thickness which is half the thickness of the steel sheet. [3] 3. The screen according to claim 1, characterized in that the deforming zone is made of an open profile with a wall thickness which is half the thickness of the steel sheet. [4] 4. The screen according to claim 1, characterized in that the deforming zone is made in the form of steel sheets with a relative elongation at more than 2% of the thickness, which is half the thickness of the steel sheet, located outside the plane, located under the cathode of the MI block and connected to the steel sheet by a continuous weld. [5] 5. The screen according to claim 1, characterized in that it is provided with an additional protective tool made of thin steel sheets with a thickness of less than 5 mm, superimposed one on another and located between the base of the cathode blocks and the main steel sheet. [6] 6. The screen according to PP.1 - A, characterized in that it. provided with an additional protective device, made in the form of a steel lining, connected to each cathode rod of the weld and electrically in contact with more than 50% of the bottom surface of the corresponding cathode block. eight I 235 With so t 2 Phie. 7 zfOl .- .; .:. ;; ...; : x; --.- .-- -: /, .. /// .. / .. I + + + fSy -f -. + + -I- + + 4 - h -) - + -h-f + + 4- -t- y + + 4- + -I- + + 4 - I- + h -) - + + 1 - (. + - n + 4- + f - - i-f + + + - (- 4+ ff + + -l - f + f + - + 4-A Ht -t- + + 2 /, Fig r2 - - ISULG t C Vft. yOvNJ.-.-. -. . x s x x chxhvcch vh l.-.-. Sh.) ShtSh: Sh; fШ Ш; .five NS SSN OC-CN VX NNS NN: / - - ISULG t C Vft. yOvNJ.-.-. .-.-. .five Par.u ////////////. Y ////////////// tPuz.ff Compiler A.Lyutikov Editor A.Lezhnina Tehred I.Popovich Proofreader N.Korol Order 7733/61 Circulation 610 Subscription VNIIPI USSR State Committee for inventions and discoveries 113035, Moscow, Zh-35, Raushsk nab., d, D / 5 Production and printing company, Uzhgorod, Projecto st., 4
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同族专利:
公开号 | 公开日 NZ208146A|1987-04-30| AU2801984A|1984-11-22| AU558957B2|1987-02-12| FR2546183B1|1985-07-05| ZA843646B|1985-07-31| EP0126700B1|1987-03-18| CA1228834A|1987-11-03| NO841929L|1984-11-19| US4488955A|1984-12-18| IS2912A7|1984-11-17| IS1280B6|1987-07-07| GR81945B|1984-12-12| FR2546183A1|1984-11-23| IN161908B|1988-02-20| ES288257U|1985-12-16| DE3462702D1|1987-04-23| EP0126700A1|1984-11-28| YU83884A|1988-04-30| ES288257Y|1986-07-16|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 FR1102097A|1954-03-29|1955-10-17|Bouchayer & Viallet Ets|Improvements to caissons used in electro-metallurgy| US3494851A|1967-05-17|1970-02-10|Kaiser Aluminium Chem Corp|Electrolytic cells| US4175022A|1977-04-25|1979-11-20|Union Carbide Corporation|Electrolytic cell bottom barrier formed from expanded graphite| CH643602A5|1979-10-17|1984-06-15|Alusuisse|ELECTROLYSIS PAN.| CH653711A5|1981-04-22|1986-01-15|Alusuisse|ELECTROLYSIS PAN.|FR2560613B2|1983-05-16|1987-03-27|Pechiney Aluminium|IMPROVEMENT ON CATHODE RATES WITH A METAL SOLE, FOR HALL-HEROULT ELECTROLYSIS TANKS| US4556468A|1984-09-26|1985-12-03|Aluminum Company Of America|Electrolytic cell| GB8520453D0|1985-08-15|1985-09-18|Alcan Int Ltd|Aluminium reduction cells| DE3538016C2|1985-10-25|1993-03-18|Vereinigte Aluminium-Werke Ag, 5300 Bonn Und 1000 Berlin, De| US5976333A|1998-01-06|1999-11-02|Pate; Ray H.|Collector bar| DE102009024881A1|2009-06-09|2010-12-16|Sgl Carbon Se|Cathode bottom, method for producing a cathode bottom and use thereof in an electrolytic cell for the production of aluminum|
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申请号 | 申请日 | 专利标题 FR8308333A|FR2546183B1|1983-05-16|1983-05-16|SUB-CATHODIC SCREEN COMPRISING DEFORMABLE AREAS, FOR HALL-HEROULT ELECTROLYSIS TANKS| 相关专利
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