DK179126B1 - COVERING SYSTEM FOR AN ELECTROLYTIC CELL - Google Patents
COVERING SYSTEM FOR AN ELECTROLYTIC CELL Download PDFInfo
- Publication number
- DK179126B1 DK179126B1 DKPA201670545A DKPA201670545A DK179126B1 DK 179126 B1 DK179126 B1 DK 179126B1 DK PA201670545 A DKPA201670545 A DK PA201670545A DK PA201670545 A DKPA201670545 A DK PA201670545A DK 179126 B1 DK179126 B1 DK 179126B1
- Authority
- DK
- Denmark
- Prior art keywords
- sealing
- caps
- electrolytic cell
- hoods
- flaps
- Prior art date
Links
- 238000007789 sealing Methods 0.000 claims abstract description 105
- 238000000034 method Methods 0.000 claims abstract description 11
- 238000000429 assembly Methods 0.000 claims description 14
- 230000000712 assembly Effects 0.000 claims description 14
- 239000000463 material Substances 0.000 claims description 11
- 239000000843 powder Substances 0.000 claims description 11
- 238000005452 bending Methods 0.000 claims description 5
- 230000000284 resting effect Effects 0.000 claims description 2
- 230000003247 decreasing effect Effects 0.000 claims 1
- 230000000630 rising effect Effects 0.000 claims 1
- 239000007789 gas Substances 0.000 description 27
- 238000005868 electrolysis reaction Methods 0.000 description 11
- 206010039509 Scab Diseases 0.000 description 10
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 5
- 238000012423 maintenance Methods 0.000 description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 239000004020 conductor Substances 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 239000011810 insulating material Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 235000004418 Durio kutejensis Nutrition 0.000 description 1
- 240000002669 Durio kutejensis Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
Classifications
-
- 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
- C25C3/22—Collecting emitted gases
-
- 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
- C25C3/08—Cell construction, e.g. bottoms, walls, cathodes
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Metals (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
This method (1) comprises hoods (2), each hood (2) comprises two opposite edges designed to rest on two opposite sides of the electrolytic cell so that each hood (2) extends from one side of the electrolytic cell to the other, above the opening (116). In addition, the system (1) is designed to have longitudinal servicing windows (6) parallel to the hoods (2). The system (1) further comprises sealing lids (8), each sealing lid (8) being movable relative to the hoods (2) between a closed posi-tion, wherein each sealing lid (8) closes a window (6), and a servicing position, wherein each sealing lid (8) frees a passage through a window (6). The sealing lids (8) rest at least partly on the hoods (2), and are designed to be moved from the closed position to the servicing position, independently of each other, without moving the hoods (2) on which the sealing lids (8) rest.
Description
HOODING SYSTEM FORAN ELECTROLYTIC CELL
The present inventioRT®laies is a covering system for an electrolytic cell an electrolytic ceil comprising the covering system and a method for changing an anode assembly
Aluminum is conventionally produced in aluminum smelters by electrolysis using the Haii-Hérouit process.
An aluminum works traditionally includes hundreds of electrolytic cells connected in series and carrying an electrolysis current which may reach several hundreds of thousands of amperés. It is known that electrolytic ceils can be arranged transversely to the flow direction of the electrolysis current across the series.
Electrolytic cells conventionally comprise a steel pot shell within which there is a lining of refractory materials, a cathode of carbon materia!, through which pass cathode conductors designed to collect the electrolysis current at the cathode to route it to the cathode outputs which pass through the bottom or sides of the pot shelf, linking conductors extending substantially horizontally to the next ceil from the cathode outputs, an electrolyte bath in which the alumina is dissolved, at least one anode assembly comprising at least one anode immersed in this electrolyte bath and an anode rod sealed in the anode, an anode frame on which the anode assembly is suspended via trieanode rod, and risers for the electrolysis current running upwards connected to linking conductors from the preceding electrolytic ceil to route the electrolysis current from the cathode outputs to the anode frame and the anode assembly and anode in the next cell. The anodes are more particularly of the pre-baked anode type with pre-baked carbon blocks, i.e. baked before they are placed in the electrolytic cell.
The anode assemblies are consumed in the course of the electrolysis reaction and have to be periodically replaced with new anode assemblies.
The sides of the electrolytic cel! define an opening through which the anode assemblies are inserted into the electrolytic cell to be immersed in the electrolytic bath or extracted from the electrolytic cell to be replaced.
To limit heat loss and prevent the diffusion out of the electrolytic cell of gases generated during the electrolysis reaction, hereinafter called ceil gases, provision is made to close the opening defined by the electrolytic ceil with a covering system.
Known covering systems, such as those disclosed in patent documents US4043892 and W02007087061, comprise lateral, removable hoods, tilted relative to the horizontal. These hoods rest on one side of the electrolytic cell and also against a portion of superstructure, designed to support the anode assemblies, extending In a longitudinal direction of the electrolytic ceil, above the opening defined by the sides of the cell i.e. directly above the anode assemblies and the electrolytic bath.
Ihe hoods thus form a confinement chamber that limits the diffusion of gases when the covering system is completely closed. This also reduces heat losses.
However, during an operation requiring the covering system to be opened, as is the case for replacing a spent anode assembly by a new anode assembly, conventional covering systems offer a limited response to the problem of gases diffusing out of the electrolytic cell and the preservation of foe thermal equilibrium of foe electrolytic ceil
During an operation such as changing an anode assembly, the hoods are removed to create an opening through the covering system. This opening - a necessary one - allows access to the inside of the cell, in particular to remove a spent anode assembly. However, the opening thus created allows cell gases to diffuse outside the confinement chamber. This opening may also disturb the thermal equilibrium of the ceil.
The larger the opening thus created, the greater the amount of ceil gases that can escape, and the greater the potential heat losses. The same is true for the time during which the covering system is open during an operation: the longer the covering system remains open, foe greater the amount of ceil gas that can escape, and the greater the disturbance to the thermal equilibrium of the ceil
Given the presence, above the pot shell, of a superstructure on which the hoods of conventional covering systems are supported, the hoods that have been removed to create the opening required for the operation are often placed next to the electrolytic cell, especially in a space between celis separating two adjacent ceils. This can cause a problem of congestion, and this congestion probiem can slow down the operation, i.e, increase the length of time the covering system remains open, it can also cause a safety problem:, in that an operator may stumble.
In addition, the hoods of known covering systems are designed to have their adjacent edges overlapping each other. This overlap limits cel! gas ieaks and energy losses at the interface between two adjacent hoods.
However, conventional solutions with overlapping hoods have a disadvantage: the hoods are interlocked with each other, and the removal of one of them requires one or more adjacent hoods to be moved or removed, it is therefore clear that, for maintenance work theoretically requiring a single hood to be removed, several hoods must be moved or removed. The open area through the covering system is then larger than necessary. From patent documents US4043892 and W02007067061 we ieam of the removal of hoods in groups of three.
Finally, some maintenance operations may require smaller open areas than for other maintenance operations. For example, to break the crusts generated in the electrolytic bath during the electrolysis reaction, it is sufficient to have an opening large enough to insert a suitable tool to break these crusts at the right place while to extract or set up an anode assembly requires a larger opening suited to ihe size of the anode assembly to be extracted or set up.
However, the hoods of conventional covering systems are similar, especially in terms of dimensions, so that the only way of selecting an opening area through the covering system is to select the number of hoods to be removed. This does not allow for fine adjustment of the opening area, i.e. the selection of a minimum but sufficient opening area for performing a given maintenance operation.
Furthermore, the presence of the superstructure and risers for the electrolysis current above the opening defined by the sides of the cel! makes it difficult to break the crusts formed between the anode assemblies because access under the superstructure and the current risers is particularly cramped. It follows that crust breaking operation, conventionally performed with a chipping hammer mounted on an arm with angular inclination requires more time than if there were no such obstacles, which increases the time during which the covering system is open. In addition, because of this accessibility problem, breaking the crust is sometimes incompiete around the edges of the anode assembly and the anode assembly extracted has solid crust pieces that increase its section and its dimensions, and may damage the adjacent hoods still in place.
Finally, the lower parts of the hoods rest on on top of the pot shell on which the anode covering material collapses, so that the supports of the hoods are unstable and their positioning inaccurate. They are also exposed at the bottom part to the flames and hot spots associated with discontinuities in ihe anode covering, causing them to deteriorate rapidly.
The present invention therefore aims to overcome some or all of these drawbacks by proposing a covering system, an electrolytic cell comprising this covering system and a method for changing an anode assembly, making it possible to effectively contain the diffusion of cell gas and to maintain thermal equilibrium, in particular during a maintenance operation.
To this end, the present invention relates to a covering system for sealing an opening defined by the sides of an electrolytic cell, the covering system comprising a plurality of hoods, characterized in that: each hood comprises two opposite heating edges designed to rest on two opposite sides of the electrolytic cell from the sides of the electrolytic cel! defining the opening, so that each hood extends from one side of the electrolytic cell to the other, above the opening, the covering system is designed to have, substantially parallel to the hoods, longitudinal servicing windows to free a predetermined path through the plurality of hoods the covering system further comprises sealing lids, each sealing lid being movable relative to the hoods between a closed position, wherein each sealing lid closes one of the servicing windows, and a servicing position, wherein each closing cover frees a passage through the covering system via one of the servicing windows, the sealing lids being designed to rest at least partly on the hoods, and the sealing lids are designed to be moved from the closed position to the servicing position, independently of each other, without moving the hoods on which the sealing lids rest.
The covering system according to the Invention therefore offers the possibility of accessing the inside of the electrolytic cell by removing only one of the sealing lids, without movi ng or removing the hoods.
This makes it possible to form an opening of contained dimension through the covering system while leaving the hoods in place. For an operation such as an anode assembly change, this allows for certain preliminary operations, such as sawing through crusts formed around the anode assembly consumed during the electrolysis reaction, with a minimum open surface area through the covering system.
This limits the discharge of cell gas outside the electrolytic ceil and prevents disturbance to the thermal equilibrium of the electrolytic cell.
Opposite sides of the electrolytic ceil means the sides located on either side of a median plane especially a longitudinal median plane of the electrolytic ceil, in this way. each hood is designed to extend on either side of this median plane to rest simultaneously on these two opposite sides.
The hoods and sealing lids have a vertical assembly travel, which has a significant advantage with a view to automating the installation of the hoods, because there are no complex angular movements to be made, in contrast to the state of the art.
According to a preferred embodiment, the sealing lids have longitudinal edges which are designed to rest on each one of the hoods. Sealing at the junction between the sealing lids and the hoods is provided over the entire length of the hoods, and tie sealing isds respectively, by overlapping one edge of the sealing || over oho edge of the hood.
According toa preferred ^ have a T-shaped cross-section defining two longitudinal flanges, tie hoods have a cross-section in the shape of an inverted T delimiting two longitudinal flanges, each flange of one of the sealing lids resting on one of the flanges of an adjacent hood, so that the covering system has an alternation of interlocking hoods and sealing lids.
This configuration provides a simple solution to enable removal of the sealing lids without interfering with the hoods on which they rest and the other sealing lids, and at the same time to improve the sealing of the covering system. This makes it possible to limit the leakage of cell gas and heat losses.
Advantageously, the flanges of the hoods and sealing lids have an L-shaped section, so that the interlocking of a hood and a sealing lid forms a sealing baffle.
This feature also provides the advantage of an improved seal, containing ceil gas leakage and heat loss.
Advantageously, the covering system comprises sealing means interposed between the flanges of each sealing lid and the flanges of the adjacent hoods on which each sealing Sid rests.
Sealing is thereby improved.
According to an advantageous embodiment, the hoods and lids extend horizontally and the longitudinal flanges of the hoods comprise channels containing a powder material and having a top opening, the longitudinal flanges of the lids having an L-shaped section, so that an end portion of the L-shaped section of the lid is pressed into the powder material through the top opening in the channel when the hood and the lid are interlocked. Making such a seal by means of a powder materia! is possible because the hoods and lids extend horizontally so that the powder material remains distributed with a uniform height throughout the length of the channel . The powder materia! forms a barrier preventing cell gas from escaping.
Advantageously, the powder material contains alumina. More particularly, the powder material may be formed of alumina or crushed electrolytic bath comprising alumina. These materials have the advantage of being available in an aluminum works and are additionally introduced into the electrolytic cells so they are not likely to pollute the electrolytic ceil in the event of accidental spillage in the celt. In addition, alumina is a very good adsorbent for the HF and S02 generated by the electrolytic cell so that any infiltration of ceil gas through the powder mate rial wiii havea Sesser environmental impact.
Advantageously, the hoods and / or iids comprise a shutter arranged to close the opening of the channel when the hood and the lid are interlocked, lie purpose of this shutter, which can be fixed or mobile, especially swiveling, is to retain the powder material in the channel.
According to an advantageous embodiment, the sealing means comprise elastic seals designed to compensate for a difference in relative deformation between two consecutive hoods of the covering system between which a sealing lid in closed position is designed to extend. in other words, the space or clearance between hoods arid sealing lids Is sized so that flattening of the seals separating them, taking into account the bending of the hoods and sealing lids, fails within the elastic range of flattening of the seals. Sealing is thereby improved.
According to an advantageous embodiment, the hoods inciude a surface provided with at least one reinforcing rib designed to limit bending of the hoods.
This stiffens the hoods. In this way, flattening of seals is relatively uniform. Sealing is thereby improved.
According to a preferred embodiment, the hoods include a surface provided with thermal insulation means.
This helps reduce heat loss through the hood system.
Preferably, the insulating means are arranged on the underside of the hoods in order to limit distortion and thereby degradation of the hoods.
Advantageously, the hoods include a substantially longitudinal tubular body, the tubular body defining a cavity within which is arranged a thermally insulating material.
These features help protect the thermally insulating material and limit heat losses, by synergistic effect between the thermally insulating material, which slows the spreading of heat through the covering system and the improved rigidity of the hoods due to the tubular nature of the body, this rigidity aliowing the hood to bear uniformiy against the surface on which it rests and the sealing lids to bear uniformly on this hood.
According to a preferred embodiment, the hoods comprise a lower surface provided with deflection means for deflecting a flow of ceil gas.
Ceil gases can be diverted toward a capture system that the electrolytic cell can be equipped with, so that cell gas leaks are limited.
According to a preferred embodiment, the sealing lids comprise gripping means designed to allow substantially vertical lifting of each sealing lid without moving the hoods and independently of the other sealing lids.
Substantially vertical removal of the sealing lids limits the risk of moving adjacent hoods during withdrawal and is the easiest solution to implement a sealing system between the sealing lids and the hoods adjacent to them.
According to an advantageous embodiment, the sealing lids comprise a lower bearing surface designed to allow the sealing lids to rest stably on one of the hoods or on another sealing lid.
The sealing lids, when removed, may therefore be stacked on an adjacent hdbd Of on another nearby sealing Sid. Consequently, the trajectories described by the pot tending machine during an operation are minimal, so that the opening time of the servicing window is also minimal. This results in a reduction in cell gas leaks and heat losses that are likely to occur during an operation.
According to a preferred embodiment, the hoods comprise a bottom bearing surface designed to allow the hoods to rest stably on one of the sealing lids.
The hoods, when removed, may therefore be stacked on an adjacent hood or on another nearby sealing lid. This reduces the trajectories described by the pot tending machine, and therefore the opening time of the servicing window. Cell gas leakage and heat losses during the operation, in particular when changing an anode assembly, are lower.
According to a preferred embodiment, the hoods and the sealing lids extend in a substantially horizontal plane.
It is therefore easier to stack them quickly during an operation, which reduces the duration of the operation, and thereby the opening time of the covering system.
Advantageously, the servicing window has a width less than that of the hoods that the servicing window separates.
This small opening surface area of the cover means makes it possible to create, in combination with the conventional suction of cell gases, a suction effect of external air towards the inside of frii cell, against the movement of the cell gases. Cell gas leaks are thereby limited .
Aiso, each sealing lid has a width less than the width of the hoods.
Preferably, the hoods have a bending stiffness greater than that of the sealing lids, in other words, the hoods are more difficult to bend than the sealing lids, and the sealing lids are easier ίο bead than the hoods due to their weight, so that the sealing lids can bend to compensate for the lesser bending of the hoods on which they rest. This improves sealing
The present invention also relates to an electrolytic cell comprising a plurality of anode assemblies, sides defining an opening through which anode assemblies are designed to be set up or withdrawn with a respectively ascending or descending vertical translational movement, and a covering system having the above characteristics, the covering system extending above the anode assemblies in order to cover said opening.
This electrolytic cell has a stable thermal equilibrium and limits cell gas emissions, including during servicing work such as anode assembly replacements.
According to a preferred embodiment, the electrolytic cell comprises sealing means interposed between the bearing edges of the hoods and the sides of tie electrolytic ceil on which the bearing edges rest.
Sealing is thereby improved. Cell gas leaks are prevented and heat loss limited.
Advantageously, the sealing means, interposed between the bearing edges of ihe hoods and the sides of the cell upon which the bearing edges rest, comprise a seal, and the electrolytic cel! comprises means for pinching the seal.
This makes it possible to correct possible defects in flatness of the hoods and optionally the sealing lids, in order to limit celt gas leakage and heat loss.
According to a preferred; embodiment, each sealing lid extends above and along a subjacent space between anodes separating two adjacent anode assemblies of the electrolytic cell.
It is therefore possible to provide access in line with the space between anodes, so that an operation such as crust sawing can be achieved with a minimum open area. This operation, prior to changing an anode assembly is therefore performed with a minimum of ceil gas leakage and heat loss.
Space between anodes means space between two adjacent anode assemblies.
According to a preferred embodiment, each hood extends above arid along a subjacent anode assembly of the electrolytic cell.
It is therefore necessary to remove the covers only when an anode assembly has to be removed. The rest of the time, the hoods can remain in place to prevent cel! gas leaks and to limit heat loss. This configuration also greatly minimizes the risk of operating personnel falling into the cell.
Still according to the embodiment of figures 12 to 14, the second sealing lid 8b is initially arranged on the other side of one of the hoods 2, particularly the hood 2 where the first sealing lid 8a, if appropriate, is not placed, next to which hoods the first sealing lid 8a was arranged so that a second passage is freed on the other side of this hood 2. in addition, the method indudes a step involving breaking or sawing a crust formed on the surface of the electrolytic bath 110, by inserting a suitable too! for breaking or sawing the crust around this second passage,
Stiil according to the embodiment of figures 12 to 14, the method may include a step involving placing the second sealing lid 8b on the first sealing lid 8a, as is particularly visible in figure 13,
As can be seen in figure 14 the method further comprises a step involving withdrawal of one of the hoods 2 initially arranged beside the first sealing lid 8a, particularly hood 2 where the first sealing iid 8a, if appropriate, is not placed.
The method may comprise an additional step involving stacking this hood on the second sealing iid 8b.
Note that the first and if appropriate the second sealing iid 8a, 8b and the hood 2 are stacked above an unchanged anode assembly 109.
The method may then inciude a step involving extraction of the spent anode assembly 130, below the previously removed hood 2, and a step involving inserting the new anode assembly inside the electrolytic ceil.
These steps can be performed by substantially upward or downward vertical translation, of the spent anode assembly 130 and the new anode assembly respectively.
Finally, the method may comprise a step involving repositioning the previously removed hood 2, and then the first and second sealing lid 8a, 8b.
It will be noted that movement of the first sealing ltd 8a and of the second sealing iid 8b and of the hood 2, is achieved by means of a pot tending machine, such as a handling crane, suitable for approaching these shutter covers 8 and the hood with their gripping means.
Claims (16)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1400177A FR3016890B1 (en) | 2014-01-27 | 2014-01-27 | COILING SYSTEM FOR ELECTROLYSIS TANK |
PCT/IB2015/000070 WO2015110903A1 (en) | 2014-01-27 | 2015-01-23 | Hooding system for an electrolytic cell |
Publications (2)
Publication Number | Publication Date |
---|---|
DK201670545A1 DK201670545A1 (en) | 2016-09-05 |
DK179126B1 true DK179126B1 (en) | 2017-11-20 |
Family
ID=50489286
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DKPA201670545A DK179126B1 (en) | 2014-01-27 | 2016-07-19 | COVERING SYSTEM FOR AN ELECTROLYTIC CELL |
Country Status (9)
Country | Link |
---|---|
EP (1) | EP3099841B1 (en) |
CN (1) | CN105934537B (en) |
AU (1) | AU2015208857B2 (en) |
BR (1) | BR112016015587B1 (en) |
CA (1) | CA2935478C (en) |
DK (1) | DK179126B1 (en) |
FR (1) | FR3016890B1 (en) |
RU (1) | RU2682498C2 (en) |
WO (1) | WO2015110903A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107099821B (en) * | 2017-06-23 | 2023-07-25 | 重庆科技学院 | Full sealing device for upper part of prebaked anode aluminum electrolytic cell |
EP4174216A1 (en) * | 2021-10-27 | 2023-05-03 | Dubai Aluminium PJSC | Protection device for anodes of an electrolytic cell, comprising movable panels, and its implementation method |
CN114318366B (en) * | 2021-12-02 | 2024-01-30 | 珠海格力电器股份有限公司 | Electrolysis generating device |
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Publication number | Priority date | Publication date | Assignee | Title |
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US3935090A (en) * | 1974-03-15 | 1976-01-27 | Dmitry Pavlovich Petrusenko | Covering of an aluminum-producing electrolysis cell |
US4043892A (en) * | 1975-12-15 | 1977-08-23 | Reynolds Metals Company | Aluminum reduction cell having a lateral enclosure system |
US4218300A (en) * | 1978-08-24 | 1980-08-19 | Swiss Aluminium Ltd. | Covering for a cell for fused salt electrolysis |
WO2007067061A1 (en) * | 2005-12-09 | 2007-06-14 | Norsk Hydro Asa | A method and a device in connection with handling covers in a superstructure in an electrolytic cell |
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US2822328A (en) * | 1953-07-20 | 1958-02-04 | Henry J Kaiser Company | Bifurcated self-baking anode and gas collection means |
NO168542C (en) * | 1989-05-24 | 1992-03-04 | Elkem Aluminium | DEVICE FOR GAS COLLECTION IN OVENS FOR MELT ELECTROLYTIC ALUMINUM PREPARATION. |
NO172250C (en) * | 1990-05-07 | 1993-06-23 | Elkem Aluminium | DEVICE FOR CLOSING THE ANODETOPE ON A SODER BERGANODEI AN ELECTROLYCLE CELL FOR ALUMINUM PRODUCTION |
DE4118304A1 (en) * | 1991-06-04 | 1992-12-24 | Vaw Ver Aluminium Werke Ag | ELECTROLYSIS CELL FOR ALUMINUM EFFICIENCY |
CN2114667U (en) * | 1992-02-15 | 1992-09-02 | 贾石明 | Cover door for safety ceal aluminium electrolyte bath |
NO179415C (en) * | 1994-02-21 | 1996-10-02 | Elkem Aluminium | Method and apparatus for closing and cooling the top of the anode sheath on a Söderberganode in an electrolytic cell for the production of aluminum |
NO310730B1 (en) * | 1999-11-17 | 2001-08-20 | Norsk Hydro As | Method and apparatus for operation of electrolysis cell |
EP1303649B1 (en) * | 2000-07-19 | 2012-08-29 | Alcoa Inc. | Insulation assemblies for metal production cells |
RU2294407C1 (en) * | 2005-06-08 | 2007-02-27 | Открытое акционерное общество "Всероссийский алюминиево-магниевый институт" | Shelter for aluminum cell with fired anodes |
RU2385974C2 (en) * | 2007-10-19 | 2010-04-10 | РУСАЛ АйПи ХОЛДИНГ ЛИМИТЕД | Cover of aluminium electrolyser with burnt anodes |
FR2953223B1 (en) * | 2009-12-02 | 2012-01-27 | Alcan Int Ltd | METHOD FOR CHANGING A WEEE ANODE AND SUPPORT AND SYSTEM FOR TEMPORARILY STORING SUCH A WASTE ANODE |
-
2014
- 2014-01-27 FR FR1400177A patent/FR3016890B1/en not_active Expired - Fee Related
-
2015
- 2015-01-23 AU AU2015208857A patent/AU2015208857B2/en active Active
- 2015-01-23 WO PCT/IB2015/000070 patent/WO2015110903A1/en active Application Filing
- 2015-01-23 EP EP15740112.6A patent/EP3099841B1/en active Active
- 2015-01-23 RU RU2016134372A patent/RU2682498C2/en active
- 2015-01-23 BR BR112016015587-4A patent/BR112016015587B1/en active IP Right Grant
- 2015-01-23 CA CA2935478A patent/CA2935478C/en active Active
- 2015-01-23 CN CN201580005849.0A patent/CN105934537B/en active Active
-
2016
- 2016-07-19 DK DKPA201670545A patent/DK179126B1/en active
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BR112016015587A2 (en) | 2017-08-08 |
RU2016134372A3 (en) | 2018-10-04 |
CA2935478A1 (en) | 2015-07-30 |
EP3099841A1 (en) | 2016-12-07 |
FR3016890B1 (en) | 2016-01-15 |
RU2682498C2 (en) | 2019-03-19 |
EP3099841A4 (en) | 2017-11-08 |
DK201670545A1 (en) | 2016-09-05 |
AU2015208857B2 (en) | 2018-08-16 |
WO2015110903A1 (en) | 2015-07-30 |
CA2935478C (en) | 2021-11-23 |
AU2015208857A1 (en) | 2016-07-28 |
FR3016890A1 (en) | 2015-07-31 |
CN105934537A (en) | 2016-09-07 |
CN105934537B (en) | 2018-01-05 |
BR112016015587B1 (en) | 2022-01-25 |
RU2016134372A (en) | 2018-03-02 |
EP3099841B1 (en) | 2019-07-24 |
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