SU908959A1 - Electrolyzer - Google Patents
Electrolyzer Download PDFInfo
- Publication number
- SU908959A1 SU908959A1 SU802894932A SU2894932A SU908959A1 SU 908959 A1 SU908959 A1 SU 908959A1 SU 802894932 A SU802894932 A SU 802894932A SU 2894932 A SU2894932 A SU 2894932A SU 908959 A1 SU908959 A1 SU 908959A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- electrolyzer
- cavities
- heat
- heat exchanger
- sides
- Prior art date
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Electrolytic Production Of Metals (AREA)
Description
(54) ЭЛЕКТРОЛИЗЕР ДЛЯ ПОЛУЧЕНИЯ АЛЮМИНИЯ(54) ELECTROLIZER FOR ALUMINUM PRODUCTION
II
Изобретение относитс к цветной металлургии , в частности к устройствам дл стабилизации энергетического режима и утилизации тепла электролизеров дл получени алюмини .The invention relates to non-ferrous metallurgy, in particular, to devices for stabilizing the energy regime and heat recovery of electrolyzers for producing aluminum.
Известен электролизер дл получени алюмини с устройством дл стабилизации температурного режима и утилизации тепла катодного и анодного кожухов 1.A known cell for producing aluminum with a device for stabilizing the temperature and heat recovery of the cathode and anode housings 1.
Недостатком вл етс нестабилизироваиный тепловой режим.The disadvantage is unstabilized thermal conditions.
Наиболее близким к предлагаемому вл етс электролизер дл получени алюмини , включающий анодное, катодное устройства с герметичными полост ми, кожух с днищем и бортами, устройство дл утилизации тепла и магистрали теплоносител (2.The closest to the present invention is an electrolysis cell for producing aluminum, including an anodic, cathodic device with hermetic cavities, a casing with a bottom and sides, a device for heat recovery and a heat carrier (2.
Недостатками известного электролизера вл ютс нестабильность теплового режима и невозможность полного утилизации тепла.The disadvantages of the known electrolyzer are the instability of the thermal regime and the impossibility of complete heat recovery.
В известном электролизере предусмотрены герметичные полости в зонах катодного и анодного кожухов, соединенные магистрал ми дл движени теплоносител , например возду ,ха, от вентил тора наддува, и теплообменНИК после электролизера дл утилизации тепловых потерь его элементов. При этом, поток воздуха после вентил тора с помощью воздухораспределительных устройств распредел етс на полости в зонах анода и катодного кожуха, раздел сь далее параллельными потоками на борта и днище электролизера . При этом в полости катодного кожуха поступает атмосферный воздух с температурой окружающей среды. При использовании ли10 нии рециркул ции нагретого в полостн днища воздуха на всас вентил тора потребуетс установка дополнительного вентил тора с соответствующим количеством труб.Sealed cavities in the areas of the cathode and anode housings, connected by pipes for movement of the coolant, for example air, from the pressurization fan, and heat exchanger after the electrolyzer for utilization of heat losses of its elements are provided in the known electrolyzer. At the same time, the air flow after the fan is distributed to the cavities in the zones of the anode and the cathode casing by means of air-distributing devices, further divided by parallel flows to the beads and the bottom of the electrolyzer. At the same time, atmospheric air with ambient temperature enters the cavity of the cathode jacket. When using recirculation of heated air in the bottom of the air in the suction side of the fan, an additional fan with an appropriate number of pipes will be required.
1515
Более целесообразным вл етс подача воздуха после вентил тора в полости в зоне бортов, а из них - в полости в зоне днища , т.е. последовательна схема движени теплоносител . Однако при этом по вл ютс More appropriate is the supply of air after the fan in the cavity in the area of the sides, and of them in the cavity in the area of the bottom, i.e. consistent flow pattern of the coolant. However, there will be
20 избытки тепла с потоком от элементов электролизера.20 excess heat with the flow from the elements of the electrolyzer.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU802894932A SU908959A1 (en) | 1980-03-18 | 1980-03-18 | Electrolyzer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU802894932A SU908959A1 (en) | 1980-03-18 | 1980-03-18 | Electrolyzer |
Publications (1)
Publication Number | Publication Date |
---|---|
SU908959A1 true SU908959A1 (en) | 1982-02-28 |
Family
ID=20883065
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU802894932A SU908959A1 (en) | 1980-03-18 | 1980-03-18 | Electrolyzer |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU908959A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1989006289A1 (en) * | 1987-12-28 | 1989-07-13 | Aluminum Company Of America | Electrolytic cell and process |
US5015343A (en) * | 1987-12-28 | 1991-05-14 | Aluminum Company Of America | Electrolytic cell and process for metal reduction |
-
1980
- 1980-03-18 SU SU802894932A patent/SU908959A1/en active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1989006289A1 (en) * | 1987-12-28 | 1989-07-13 | Aluminum Company Of America | Electrolytic cell and process |
US5015343A (en) * | 1987-12-28 | 1991-05-14 | Aluminum Company Of America | Electrolytic cell and process for metal reduction |
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