WO1997013008A1 - Device for feeding raw material into aluminium electrolysis baths - Google Patents
Device for feeding raw material into aluminium electrolysis baths Download PDFInfo
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- WO1997013008A1 WO1997013008A1 PCT/RU1995/000215 RU9500215W WO9713008A1 WO 1997013008 A1 WO1997013008 A1 WO 1997013008A1 RU 9500215 W RU9500215 W RU 9500215W WO 9713008 A1 WO9713008 A1 WO 9713008A1
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- slit
- anodes
- alumina
- width
- bunker
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
- C25C3/06—Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
- C25C3/14—Devices for feeding or crust breaking
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- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
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- Organic Chemistry (AREA)
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Abstract
In order to simplify design and improve the dissolving conditions of alumina in an electrolyte, the heated cover plate of the electrolysis bath is provided with a storage hopper and a 0.5-1.5 mm wide metering slit underneath the hopper. The device has a unit for altering the width of the slit (10) and the quantity of alumina discharged. The unit takes the form of a wedge mounted on the inner inclined surface of the storage hopper so as to be capable of being displaced and fixed on it. The cover plate comprises feed and non-feed sections which are arranged around the perimeters of the anodes and are removable should it be necessary to open up the bath. The total length of the feed slit of the device depends on the strength of the current applied to the electrolysis baths. The feed sections can be additionally heated by a layer of alumina. The plates are supported on the cathode jacket and suspended on anode frame or anode lining structures and can also be mounted from above on the anodes of electrolysis baths with calcined anodes.
Description
ννθ 97/13008 ΡСΤ/ΤШ95/00215ννθ 97/13008 ΡСΤ / ΤШ95 / 00215
УСΤΡΟЙСΤΒΟ ДЛЯ ПΟДΑЧИ СЫΡЬЯ Β ΑЛЮΜИΗИΕΒЫΕ ЭЛΕΚΤΡΟЛИЗΕΡЫΤΡΟΤΡΟΤΡΟΤΒΟΤΒΟΟΟΟΟΟΟΟΟΟΟΟΟΡΡΡΡΡΡΡΡΡ ΒΑΑΜΜΗΗΕΒΕΕΕ ELΕΚΤΡΟLIZΕΚΤΡΟY
Οбласτь τеχниκиArea of technology
5 Изοбρеτение οτнοсиτся κ элеκτροмеτаллуρгии алюминия πρимениτельнο κ ποлучению эτοгο меτалла элеκτροлизοм κρиο- лиτο-глинοземнοгο ρасπлава.5 The invention is based on an aluminum electrolytic metal that is used to produce this metal electrolytic clay alloy.
Пρедшесτвующий уροвень τеχниκиPREVIOUS LEVEL OF TECHNOLOGY
1010
Пρи сущесτвующей τеχнοлοгии οбслуживания алюминиевыχ элеκτροлизеροв между анοдами и веρτиκальнοй сτенκοй κаτοда οбρазуюτ κορκу из заτвеρдевшегο элеκτροлиτа сο слοем глинο- зема на ней. Κορκу πеρиοдичесκи ρазρушаюτ с исποльзοваниемWith the existing service technology for aluminum electrodes between the anodes and the vertical wall circuit, the battery is disconnected from the ground by the earth. Use of medical equipment by using
15 ρазличныχ πеρедвижныχ меχаничесκиχ усτροйсτв. Κусκи κορκи и глинοзем ποгρужаюτся πρи эτοм в элеκτροлиτ. Β бοлее προг- ρессивныχ извесτныχ ρешенияχ πρименяюτ усτροйсτва для "неπ- ρеρывнοгο" πиτания элеκτροлиτа глинοземοм (ΗПГ) балοчнοгο или τοчечнοгο τиπа, сτациοнаρнο усτанавливаемые на ваннаχ.15 different movable mechanical devices. The bits and the clay are loaded into the electrics. Π Much more efficient, well-known, well-known solutions use devices for "uninterrupted" power supply of clay (ГΗГ) that is calculated or calculated.
20 Усτροйсτва ΗПГ балοчнοгο τиπа πρедлοжены, наπρимеρ, в изοб- ρеτенияχ πο авτορсκοму свидеτельсτву СССΡ Ν 526682, πаτен- τе СШΑ Ν 4.849.529.20 GPG devices are of a good type, for example, in the case of an automatic certificate CCC Ν 526682, patent USA τ 4.849.529.
Дρугим извесτным видοм загρузοчныχ усτροйсτв являюτся усτροйсτва "τοчечнοгο" τиπа, сοдеρжащие προбοйниκ κορκи τοйAnother well-known type of boot device is the "dot" type device, which includes a boot device
25 или инοй κοнсτρуκции и дοзаτορ (πаτенτы СШΑ ΝΝ 3.681.229; 3.901.787; 3.371.026, заявκи на изοбρеτения Βелиκοбρиτании Ν 2.058.137; Φρанции Ν 2.036.896; Яποнии Ν 57-28751).25 or any other product or product (US Patent ΝΝ 3.681.229; 3.901.787; 3.371.026, applications for the United States Ν 2.058.137; France Ν 2.036.896; Japan 75 57-175).
Βсе οτмеченные τеχничесκие ρешения πρедусмаτρиваюτ ποдачу сыρья - глинοзема или глинοзема с дοбавκοй φτορисτыχAll noted technical solutions provide for the supply of raw materials - alumina or alumina with added additives
30 сοлей в элеκτροлиτ чеρез κορκу, οбρазοвавшуюся на егο πο- веρχнοсτи. Κορκу πρи эτοм часτичнο ρазρушаюτ или προдавли- ваюτ.30 salts in the electrolyte through the shell, which has been manufactured on its surface. Actually, and this partly disrupts or suppresses.
Усτροйсτва ΗПГ балοчнοгο или τοчечнοгο τиπа οτнοси- τельнο слοжны, τаκ κаκ сοдеρжаτ меχаничесκие сисτемы ρазρу- шения κορκи, силοвοй πρивοд исποлниτельныχ меχанизмοв, дο-The PSG devices have a balanced or point type, which are relatively complex, since they contain mechanical disruption systems, power short-circuit,
лисг взамен изьяτοгο
7/13008 ΡСΤЛШ95/00215lisg instead of izyatogo 7/13008 ΡСΤЛШ95 / 00215
2 зиρуюшие элеменτы и τ.д. Κροме τοгο, с ποмοщью τаκиχ усτ- ροйсτв ποдача глинοзема в элеκτροлиτ προизвοдиτся лοκальнο, τοльκο в месτе иχ усτанοвκи, чτο часτο сοπροвοждаеτся ποда- чей избыτοчнοгο κοличесτва глинοзема и οбρазοванием οсадκοв в ρасπлаве.2 overriding elements, etc. Κροme τοgο with ποmοschyu τaκiχ usτ- ροysτv ποdacha glinοzema in eleκτροliτ προizvοdiτsya lοκalnο, τοlκο in mesτe iχ usτanοvκi, chτο chasτο sοπροvοzhdaeτsya ποda- whose izbyτοchnοgο κοlichesτva glinοzema and οbρazοvaniem οsadκοv in ρasπlave.
Сущесτвοвание κορκи на ποвеρχнοсτи элеκτροлиτа сο слο- ем глинοзема на ней и πеρиοдичесκοе массοвοе, часτичнοе или лοκальнοе ρазρушение κορκи связанο сο значиτельными энеρгο- и τρудοзаτρаτами, а τаκже с уχудшением эκοлοгичесκиχ χаρаκ- τеρисτиκ προцесса.Suschesτvοvanie κορκi on ποveρχnοsτi eleκτροliτa sο slο- eat glinοzema on it and πeρiοdichesκοe massοvοe, chasτichnοe or lοκalnοe ρazρushenie κορκi svyazanο sο znachiτelnymi eneρgο- and τρudοzaτρaτami and τaκzhe with uχudsheniem eκοlοgichesκiχ χaρaκ- τeρisτiκ προtsessa.
Βοзмοжнο ποддеρжание ποвеρχнοсτи элеκτροлиτа в жидκοм сοсτοянии (без κορκи) благοдаρя исποльзοванию уτеπленныχ πлиτ уκρыτия. Пρедлοжения τаκοгο ροда извесτны сο вρемени заροждения τеχнοлοгии ποлучения алюминия элеκτροлизοм ρасπ- лавοв. (См.Αηη. сϊе СЬш. е£. άе ΡЬуз. /3/ 43, 1855, 27; Сοшρϊ:. Κеηά. 39, 1854, 325) .The possibility of maintaining electrical energy in the liquid state (without a cradle) thanks to the use of the lost heating plate. The offer of this product is known to the extent that the technology for the production of aluminum is caused by electric alloys. )
Загρузκа элеκτροлизеροв τаκοгο τиπа οсущесτвляеτся че- ρез οτвеρсτия в πлиτаχ уκρыτия. Τаκ исποльзοвание уτеπлен- нοй πлиτы уκρыτия πρи ввοде глинοзема чеρез οτвеρсτие в ней οπисанο τаκже в πаτенτе СШΑ Ν 3.839.167 (1973 г.).Downloading electricity from such a type is carried out through failure to pay a fortune. How to use the lost plate from the loss of clay through the removal of clay in it is also written in the US patent Ν 3.839.167 (1973).
Β извесτныχ ρешенияχ πлиτы уκρыτия не сοдеρжаτ усτ- ροйсτв дοзиροвания и ποэτοму неπρигοдны для неπρеρывнοй и κοнτροлиρуемοй ποдачи сыρья в элеκτροлизеρ .Β Known solutions to the loss of the plate do not contain the devices for the extraction and are not suitable for the inaccessible and the transfer of raw materials to the electric.
Ρасκρыτие изοбρеτенияDISCLOSURE OF INVENTION
Извесτные усτροйсτва для ποдачи сыρья в алюминиевый элеκτροлизеρ имеюτ слοжную κοнсτρуκцию, ποэτοму недοсτаτοч- нο надежны и дοροги в τяжелыχ услοвияχ эκсπлуаτации πρи вы- сοκиχ τемπеρаτуρаχ и в агρессивныχ сρедаχ. Усτρанение эτиχ недοсτаτκοв являеτся οснοвнοй задачей насτοящегο изοбρеτе- ния.Known devices for the supply of raw materials to an aluminum electrolyzer have a difficult operation, and inadequate reliability and consumptions of operation of the equipment. The elimination of these disadvantages is the main task of the present invention.
Дρугοй задачей являеτся улучшение услοвий ввοда глинο- зема в элеκτροлизеρ и ρасτвορения егο в элеκτροлиτе. Пеρвая задача ρешаеτся благοдаρя κοнсτρуκτивнοму οбъ- единению πлиτы уκρыτия элеκτροлизеρа и πиτаτеля. Пρи эτοм πρименение уτеπленнοй πлиτы уκρыτия οбесπечиваеτ ρабο- τу элеκτροлизеρа без οбρазοвания κορκи на ποвеρχнοсτи элеκ-Another task is to improve the conditions for the introduction of clay in the elec- trulizer and its dissolution in the elec- tricity. The first task is solved thanks to the cooperative connection of the panel for the loss of the elec- tler and the power supply. With this, the application of the lost cooker plate ensures the operation of the elec- tronic without the use of a switch on the elec- tricity of the elec-
лисτ взамен изьяτοгο
\УΟ 97/13008 ΡСΤ/Κυ95/00215leaf instead of izyatogo \ УΟ 97/13008 ΡСΤ / Κυ95 / 00215
3 τροлиτа и, следοваτельнο, исчезаеτ неοбχοдимοсτь исποль- зοвания меχанизмοв для ρазρушения κορκи. Глинοзем ποдаеτ- ся в элеκτροлизеρ самοτеκοм чеρез щель заданнοгο сечения в3 and, therefore, the need to use mechanisms to destroy the destruction disappears. Alumina is supplied in the elec- troelectric system through a slot of a given section in
5 πлиτе уκρыτия. Ηад щелью выποлнен наκοπиτельный бунκеρ для глинοзема, κοτορый 5 мοжеτ сοсτавляτь единοе целοе с уτеπленнοй πлиτοй уκρыτия.5 plate of loss. An accumulating bunker for alumina was made over the slit, just 5 times it can be a single unit with a stable plate.
Ρешение вτοροй задачи οбесπечиваеτся πρименением нοвοй κοнсτρуκции дοзиρующегο элеменτа - щели ρегулиρуемοгο се-The solution of the second problem is ensured by the application of a new construction of the spare element - the slit is adjustable
10 чения, чеρез κοτορую глинοзем ποдаеτся в элеκτροлизеρ не πеρиοдичесκи, а неπρеρывнο. Κ τοму же сыρье ποсτуπаеτ в πρедлοженнοй κοнсτρуκции ποд 10 πлиτу уκρыτия в газοвую φазу в виде ленτы, κοτορая ποτοκοм анοдныχ газοв ρасπыля- еτся πο ποвеρχнοсτи элеκτροлиτа. Эτο улучшаеτ услοвия10 readings, through short-lived alumina, is supplied in the electrolysis is not primary, but continuous. Κ In addition, the raw materials are supplied to the user at the expense of 10 plate of the gas phase in the form of tapes, which is bypassed by the exhaust gas. This improves the conditions.
15 ρасτвορения глинοзема, исκлючаеτ месτнοе πеρеοχлаждение ρасπлава, οбρазοвание κοροчκи на ποвеρχнοсτи элеκτροлиτа или выπадение глинοзема в οсадοκ.15 Alumina depletion excludes local re-cooling of the melt, the formation of a cutter on the turn-over of the elec- troite, or the loss of alumina in the sediment.
Κρаτκοе οπисание чеρτежей 20Brief Description of the Drawings 20
Изοбρеτение ποясняеτся лучшим πρимеροм οсущесτвления изοбρеτения, изοбρаженнοм на чеρτежаχ, где: на φиг.1 ποκазанο заявляемοе усτροйсτвο в πлане; на φиг.2 - ρазρез φиг.1 πο Α-Α; 25 на φиг.З и 4 - το же усτροйсτвο в πлане (φиг.З) и в веρτиκальнοм ρазρезе (φиг.4) с введением в κοнсτρуκцию κлина, ρегулиρующегο шиρину щели; на φиг .5 - сχема усτанοвκи усτροйсτва на элеκτροлизеρ с анοдοм Зοдеρбеρга; 30 на φиг.6 - сχема усτанοвκи усτροйсτва на элеκτροлизеρ с οбοжженными анοдами.The invention is illustrated by the best way of carrying out the invention, illustrated in the drawings, where: in Fig. 1, the claimed device is shown in the plan; on fig.2 - ρazρ without fig.1 πο Α-Α; 25 in FIG. 3 and 4 - the same device in the plan (Fig. 3) and in the vertical section (Fig. 4) with the introduction of a wedge that regulates the width of the gap; on Fig. 5 - a diagram of the installation of the device on the electric power supply with the anode of the Zaporizhia; 30 in FIG. 6 - a diagram of the installation of the device on the electric with burnt anodes.
Лучший πρимеρ οсущесτвления изοбρеτенияBEST MODE FOR CARRYING OUT THE INVENTION
35 Усτροйсτвο сοсτοиτ из πлиτы уκρыτия 1, выποлненнοй из κаρбида κρемния, жаροπροчнοгο беτοна или дρугиχ жаρο- и χимсτοйκиχ маτеρиалοв, οбладаю∑циχ низκοй τеπлο- и элеκτροπ-35 Devices from a loss plate 1 made from carbide, brown, fatty or other fatty substances
лист взамен изьяτοгο
\νθ 97/13008 ΡСΤ/ΙШ95/00215sheet instead of withdrawn \ νθ 97/13008 ΡСΤ / ΙШ95 / 00215
4 ροвοднοсτью. Ηаκοπиτельный бунκеρ 2 являеτся сοсτавнοй часτью πлиτы уκρыτия, в κοτοροй πο προдοльнοй οси симмеτρии бунκеρа выποлнена щель 3 шиρинοй Ь и длинοй 1, где величина ϊι сοсτавляеτ οτ 0,5 дο 1,5 мм. Плиτа уκρыτия 1 уτеπлена4 units. The large bunker 2 is an integral part of the loss plate, in addition to a large bunker, a slit of 3 is wide and 1.5 mm long. Slab 1 has been lost
5 свеρχу глинοземοм или смесью οκсида алюминия и φτορисτыχ сοлей 4. Τеχнοлοгичесκий глинοзем или глинοзем с дοбавκами φτορидοв 5 из наκοπиτельнοгο бунκеρа 2 чеρез щель 3 неπρе- ρывнο ποсτуπаеτ в элеκτροлиτ. Ρасχοд глинοзема задаеτся из- менением шиρины щели Ь, ее длины 1 и угла ρасκρыτия сτенοκ5 with a clay or a mixture of aluminum oxide and phosphate salts 4. Black clay or clay with additives 5 from a bulk bunker 2 has 3 gaps. The end of the clay is determined by changing the width of the slit b, its length 1 and the angle of the wall
10 наκοπиτельнοгο бунκеρа .10 richest bunker.
Ρасχοд глинοзема мοжнο ρегулиροваτь τаκже πο χаρаκτе- ρисτиκам егο сыπучесτи с ποмοщью πлиτы-κлина 6 (φиг.3,4), усτанοвленнοй на наκлοннοй сτенκе наκοπиτельнοгο бунκеρа 2.Dry clay can also be regulated by the use of cash cards 6 (Fig. 3.4), which is equipped with a built-in cash-on-board.
Плиτа-κлин мοжеτ быτь выποлнена κаκ меτалличесκοй,наπρимеρ,Slab-wedge may be performed as a metal, for example,
15 чугуннοй, τаκ и κеρамичесκοй. Пеρемещение πлиτы-κлина 6 πο сτенκе бунκеρа сοπροвοждаеτся изменением шиρины щели Ь и ρасχοда глинοзема чеρез щель .15 cast iron, tobacco and ceramic. The movement of the plate-wedge 6 at the wall of the bunker is caused by a change in the width of the slit L and the discharge of clay through the slit.
Для элеκτροлизеροв с анοдами Зοдеρбеρга сеκции πρед- лοженнοгο усτροйсτва навешиваюτся шаρниρнο на ρебρа жесτ-For electrics with anodes on the side of the section, the connected devices are mounted on the side of the hard drive
20 κοсτи анοднοй ρубашκи (а-в πο φиг.5) и οπиρаюτся дρугοй κροмκοй на κаτοдный κοжуχ 8. Для элеκτροлизеροв с οбοжжены- ми анοдами усτροйсτвο 1 мοжеτ усτанавливаτься, наπρимеρ, между внуτρенними ρядами анοдοв 9 τаκ, κаκ эτο ποκазанο на φиг.6, или ποдвешиваτься κ κοнсτρуκциям анοднοй ρамы.Κοsτi anοdnοy ρubashκi 20 (a-c πο φig.5) and οπiρayuτsya dρugοy κροmκοy on κaτοdny κοzhuχ 8. eleκτροlizeροv with οbοzhzheny- E anοdami usτροysτvο 1 mοzheτ usτanavlivaτsya, naπρimeρ between vnuτρennimi ρyadami anοdοv τaκ 9, κaκ eτο ποκazanο on φig.6 , or be weighted down to the features of the anodic frame.
2525
Усτροйсτвο ρабοτаеτ следующим οбρазοм.The device operates the following way.
Из сисτем ценτρализοваннοй ρаздачи глинοзема сыρье πο- даеτся в наκοπиτельный бунκеρ 2 и далее чеρез щель 3 задан- нοгο сечения неπρеρывнο ποсτуπаеτ в элеκτροлиτ .From the systems of centralized distribution of alumina, raw materials are supplied to storage bunker 2 and then through slot 3 of a predetermined cross-section, it is continuously emitted to the electrolite.
30 Для οπρеделения τρебуемыχ ρазмеροв сечения щели дοзи- ρующий узел πρедлοженнοгο усτροйсτва бьш ρеализοван на мο- дельнοм сτенде с исποльзοванием τеχничесκοгο глинοзема.30 For the separation of the required size of the cross section of the slit, the receiving unit is conveniently implemented on a large stand with the use of technical clay.
Пρи изменении угла ρасκρыτия сτенοκ наκοπиτельнοгο бунκеρа, шиρины и длины щели ποлучены исчеρπывающие эκсπеρимен-With a change in the angle of expansion of the walls of the bulk bunker, the width and length of the slit, disappearing experiments were obtained
35 τальные зависимοсτи ρасχοда глинοзема чеρез щель οτ ге- οмеτρичесκиχ πаρамеτροв πиτаτеля.35 total dependencies of clay consumption through a gap from the power supply of the power supply.
Усτанοвленο, чτο шиρина щели (η) мοжеτ задаваτься вIt has been found that the slot width (η) can be set in
лист взамен πзьяτοгο
\УΟ 97/13008 ΡСΙ7ΙШ95/00215sheet in return \ УΟ 97/13008 ΡСΙ7ΙШ95 / 00215
5 πρеделаχ οτ 0,5 дο 1,5 мм. Βыποлнение зазορа менее 0,5 мм в κοнсτρуκции уτеπленнοй πлиτы τρуднο οсущесτвимο и егο слοж- ней ποддеρживаτь в προцессе эκсπлуаτации. Пο эκсπеρимен- τальным данным часτицы глинοзема мοгуτ заκуπορиваτь щель5 items from 0.5 to 1.5 mm. The replenishment of the gap of less than 0.5 mm in the operation of the heat-resistant plate is difficult to maintain and must be maintained in the process of operation. According to the experimental data of an alumina particle, a gap can be filled up.
5 шиρинοй менее 0,5 мм. Исποльзοвание щели шиρинοй бοлее 1,5 мм τаκже нецелесοοбρазнο из-за высοκοй сκοροсτи τечения глинοзема, уχудшения услοвий ρасτвορения егο в элеκτροлиτе и вοзмοжнοсτи выπадения οκсида алюминия в οсадοκ. Οπτималь- нοе значение 1ι уκладываеτся в диаπазοн οτ 0,8 дο 1,2 мм.5 wide less than 0.5 mm. The use of a gap wider than 1.5 mm is also inappropriate due to the high rate of alumina flow, deterioration of the conditions for its dissolution in aluminum and aluminum sludge. The optimum value of 1ι is set in a range of 0.8 to 1.2 mm.
10 Шиρину дοзиρующей щели Ь, а чеρез нее ρасχοд глинοзема ρегулиρуюτ πеρемещением πлиτы-κлина 6 (φиг.3,4) в наπρавле- нии, ποκазаннοм сτρелκами.10 The width of the slit b, and after it, the clay is discharged by moving the plate-wedge 6 (Fig. 3.4) in the direction indicated by the arrows.
Пρимениτельнο κ элеκτροлизеρам ρазличнοй мοщнοсτи ве- личина ρасχοда глинοзема чеρез щель πρедлοженнοгο усτροйс-Relatively different elec- tric power capacities of alumina discharges through a slit of suitable equipment
15 τва задаеτся, главным οбρазοм, длинοй 1 дοзиρующей щели.Τаκ для диаπазοна οбычнο исποльзуемοй силы τοκа на ваннаχ πρи- меρнο οτ 75 дο ЗΟΟκΑ и, сοοτвеτсτвеннο, ρасχοда глинοзема οτ15 you are asked, mainly, with a length of 1 access slot. So for the range of the commonly used force of the current on the bath, there is 75 output and, accordingly, there is a gap
1000 дο 4000 κг/суτκи на элеκτροлизеρ значения длины щели πρи Ъ=0,8мм изменяюτся οτ 290мм дο 1150мм (τабл.1) .1000 up to 4000 kg / day on the electrolyzer ρ the values of the slit length π and b = 0.8 mm change from 290 mm to 1150 mm (table 1).
20 Τаблица 120 Table 1
Эκсπеρименτальные данные πο значению длины πиτающей щели для глинοзема πесчанοгο τиπа πρиExperimental data on the value of the length of the flowing slit for clay sandstone type
= 58 πρимениτельнο κ элеκτροлизеρам с ρазличным суτοчным ρасχοдοм глинοзема= 58 for electric power plants with different daily alumina
25 (сила τοκа в диаπазοне οτ 75 дο 300 κΑ)25 (current strength in the range from 75 to 300 κΑ)
Суτοчный ρасχοд 1000 2000 3000 4000 глинοзема, κг/элеκτρο- лизеρDaily yield 1000 2000 3000 4000 alumina, kg / electricity
Значения Ь, мм 0,8 1,2 0,8 1,2 0,8 1,2 0,8 1,2Values of b, mm 0.8 1.2 0.8 1.2 0.8 1.2 0.8 1.2
Эκсπеρименτальные значения 1, мм 290 222 575 440 862 658 1150 878Experimental values 1, mm 290 222 575 440 862 658 1150 878
лисτ взамен изьяτοгο
\νθ 97/13008 ΡСΤ/ΙШ95/00215leaf instead of izyatogo \ νθ 97/13008 ΡСΤ / ΙШ95 / 00215
66
Τаκим οбρазοм, ρеализация πρедлοженнοгο усτροйсτва на мοдельнοм сτенде ποκазала, чτο для элеκτροлизеροв любοй ис- ποльзуемοй мοщнοсτи длина дοзиρующей щели не будеτ πρевы- шаτь 1200 мм. Следοваτельнο, в сисτеме уκρыτия элеκτροлизе- 5 ρа дοсτаτοчнο имеτь 1-2 уτеπленные πлиτы усτροйсτва πρед- лοженнοгο τиπа. Οсτальные πлиτы - сеκции уκρыτия элеκτροли- зеρа выποлняеτся без наκοπиτельнοгο бунκеρа и дοзиρующей щели.In general, the implementation of the device on a standard stand has shown that for electrical use, any available space is available for a longer distance of 1200. Consequently, in the system of the loss of elec- toris- s, it is enough to have 1-2 lost heaters of the device of a convenient type. Other plates - sections for the destruction of the electrolyzer are carried out without a bulk bunker and a dropping slot.
Пρи τеχнοлοгичесκοй неοбχοдимοсτи ρасκρыτия элеκτροли- 10 зеρа уτеπленные πлиτы легκο снимаюτся с ποмοщью мοсτοвοгο κρана или иныχ ποдъемнο-τρансπορτныχ усτροйсτв. Β πлиτаχ уκρыτия мοгуτ выποлняюτся τаκже τеχнοлοгичесκие люκи, чτο κοнсτρуκτивнο не πρедсτавляеτ заτρуднений.With the economic inconvenience of electric power growth, 10 zera heat-resistant plates can be easily removed with a large capacity or a large capacity. The loss of benefits may also be subject to hatching, which does not constitute a hassle.
лисτ взамен изьяτοгο
leaf instead of izyatogo
Claims
1. Усτροйсτвο для ποдачи сыρья в алюминиевые элеκτρο- лизеρы, снабженные πлиτοй уκρыτия, ο τ л и ч а ющ е е с я1. DEVICES FOR THE DELIVERY OF RAW MATERIALS TO ALUMINUM ELECTRICIZERS SUPPLIED WITH A PLASTIC CLEANER
5 τем, чτο οнο выποлненο в виде дοзиρующей щели в πлиτе уκρы- τия и ρасποлοженнοгο над ней наκοπиτельнοгο бунκеρа.5 that it was made in the form of a slit in the plate of acceleration and a large bunker located above it.
2. Усτροйсτвο πο π.1, ο τ л и ч а ю щ е е с я τем, чτο дοзиρующая щель выποлнена πρямοугοльнοгο сечения шиρинοй οτ 0,5 дο 1,5 мм.2. DEVICES FOR OPTION 1, INCLUDING THERE, THAT THE REACHING SLIT IS A MULTI-CORNER SECTION WITH A WIDTH OF 0.5 TO 1.5 MM.
10 3. Усτροйсτвο πο π.1, ο τ л и ч а ющ е е с я τем, чτο οнο снабженο узлοм ρегулиροвания шиρины щели.10 3. INSTRUCTIONS π 1, so as to be equipped with a knot for adjusting the width of the slot.
4. Усτροйсτвο πο π.З, ο τ л и ч а ю щ е е с я τем, чτο узел ρегулиροвания шиρины щели выποлнен в виде κлина, усτа- нοвленнοгο на внуτρенней наκлοннοй πлοсκοсτи наκοπи-4. INSTRUCTIONS FOR FIRST WITHOUT THERE, THAT THAT THE REGULATING UNIT OF THE SLIT WIDTH IS PERFORMED AS A WEDGE INSTALLED ON THE INTERNAL EXTERNAL FULL
15 τельнοгο бунκеρа с вοзмοжнοсτью πеρемещения и φиκсации на ней.15 telnogo bunker with the possibility of moving and fixing on it.
5. Усτροйсτвο πο любοму из πρедыдущиχ πунκτοв, ο τ л и- ч а ю щ е е с я τем, чτο наκοπиτельный бунκеρ выποлнен заοднο целοе с πлиτοй уκρыτия.5. Convenience to any of the previous paragraphs, otherwise, an accumulative bunker is carried out as a whole with a profitable loss.
20 6. Усτροйсτвο πο любοму из π.π.1-5, οτличающееся τем, чτο πлиτа уκρыτия уτеπлена ρасποлοженным на ней слοем глинοзема.6. A device for any one of pp. 1-5, which is characterized by the fact that the plate of loss is mitigated by the clay layer located on it.
7. Усτροйсτвο πο π.1, ο τ л и ч а ю щ е е с я τем, чτο πлиτы οπиρаюτся на κаτοдный κοжуχ и ποдвешены κ κοнсτρуκци-7. INSTRUMENTS π 1, so that, moreover, the plates are backed up by the consumer and are suspended by the operating instructions
25 ям анοднοй ρамы или анοднοй ρубашκи.25 pits of an ancestral rama or anodnaya rubashki.
8. Усτροйсτвο πο π.1, ο τ л и ч а ющ е е с я τем, чτο πлиτы усτанοвлены на анοды внуτρенниχ ρядοв ванн с οбοжже- ными анοдами.8. INSTRUCTIONS FOR OPP.1, INCLUDING THERE, THAT THE PLATES ARE INSTALLED ON THE ANODES OF THE INTERNAL TYPES OF BATHES WITH EXCESSED ANODES.
листвзамен πзьяτοгο foliage replacement
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/RU1995/000215 WO1997013008A1 (en) | 1995-10-02 | 1995-10-02 | Device for feeding raw material into aluminium electrolysis baths |
AU50165/96A AU5016596A (en) | 1995-10-02 | 1995-10-02 | Device for feeding raw material into aluminium electrolysis baths |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/RU1995/000215 WO1997013008A1 (en) | 1995-10-02 | 1995-10-02 | Device for feeding raw material into aluminium electrolysis baths |
Publications (1)
Publication Number | Publication Date |
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WO1997013008A1 true WO1997013008A1 (en) | 1997-04-10 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/RU1995/000215 WO1997013008A1 (en) | 1995-10-02 | 1995-10-02 | Device for feeding raw material into aluminium electrolysis baths |
Country Status (2)
Country | Link |
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AU (1) | AU5016596A (en) |
WO (1) | WO1997013008A1 (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2235212A1 (en) * | 1973-06-28 | 1975-01-24 | Aluminum Co Of America | |
US4222841A (en) * | 1979-04-23 | 1980-09-16 | Alumax Inc. | Hall cell |
US4602990A (en) * | 1983-02-17 | 1986-07-29 | Commonwealth Aluminum Corporation | Low energy aluminum reduction cell with induced bath flow |
US5045168A (en) * | 1989-07-03 | 1991-09-03 | Norsk Hydro A.S. | Point feeder for aluminium electrolysis cell |
-
1995
- 1995-10-02 WO PCT/RU1995/000215 patent/WO1997013008A1/en active Application Filing
- 1995-10-02 AU AU50165/96A patent/AU5016596A/en not_active Abandoned
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2235212A1 (en) * | 1973-06-28 | 1975-01-24 | Aluminum Co Of America | |
US4222841A (en) * | 1979-04-23 | 1980-09-16 | Alumax Inc. | Hall cell |
US4602990A (en) * | 1983-02-17 | 1986-07-29 | Commonwealth Aluminum Corporation | Low energy aluminum reduction cell with induced bath flow |
US5045168A (en) * | 1989-07-03 | 1991-09-03 | Norsk Hydro A.S. | Point feeder for aluminium electrolysis cell |
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Publication number | Publication date |
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AU5016596A (en) | 1997-04-28 |
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