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
  • C25C3/08—Cell construction, e.g. bottoms, walls, cathodes
• • 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
• • 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
  • C25C3/16—Electric current supply devices, e.g. bus bars
• • 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
  • C25C3/20—Automatic control or regulation of cells

Definitions

• Aluminerie comprising electrical conductors of superconducting material
• the present invention relates to an aluminum smelter, and more particularly to the electrical conductor system of an aluminum smelter.
• an electrolytic cell composed in particular of a steel box, a refractory lining, and a cathode made of carbon material, connected to conductors used to carry the electrolysis current.
• the electrolytic cell also contains an electrolytic bath consisting in particular of cryolite in which is dissolved alumina.
• the Hall-Héroult process consists in partially immersing a carbon block constituting the anode in this electrolytic bath, the anode being consumed as and when the reaction progresses. At the bottom of the electrolytic cell is formed a sheet of liquid aluminum.
• aluminum production plants include several hundred electrolysis tanks. These electrolysis tanks are traversed by a high electrolysis current of the order of several hundreds of thousands of amperes.
• Some problems are common in an aluminum smelter; they consist in particular in the reduction of the costs in terms of energy consumed, of the material used to make the electrical conductors and the reduction of the bulk in order to increase the production on the same surface.
• Another problem results from the existence of a large magnetic field generated by the electrolysis current. This magnetic field disturbs the operation of the tanks whose performance it decreases. The vertical component of this magnetic field, in particular, causes the instability of the liquid aluminum sheet.
• This problem is particularly important at the ends of the electrolysis cell lines and requires a significant elongation of the electrical conductors connecting two neighboring lines or a queue end to the feed station. Such elongation of the electrical conductors generates a large size and an oversized buildings.
• FIG. 1 illustrates schematically, seen from above, an electrolytic tank 100 in which the magnetic field is self-compensating thanks to the arrangement of the conductors 101 connecting this tank 100 to the next tank 102 placed downstream.
• the conductors 101 are eccentric with respect to the tank 00 that they bypass.
• An example of magnetically self-compensated tank is known in particular from patent document FR2469475.
• Another solution for decreasing the vertical component of the magnetic field is to use a secondary electrical circuit formed by one or more metallic electrical conductors.
• This secondary electrical circuit conventionally follows the axis or axes of alignment of the electrolysis cells of the aluminum smelter. It is traversed by a current whose intensity is equal to a certain percentage of the intensity of the electrolysis current, and thereby generates a magnetic field compensating for the effects of the magnetic field created by the electrolysis current.
• the present invention aims to remedy all or part of the disadvantages mentioned above and to provide a solution to the problems encountered in an aluminum production plant by proposing an aluminum smelter whose manufacturing and operating costs are significantly reduced and with less space.
• the subject of the present invention is an aluminum smelter comprising:
• the use of at least one electrical conductor of superconducting material makes it possible in particular to reduce the overall energy consumption of the aluminum smelter, and therefore the operating costs of the smelter.
• electrical conductors of superconducting material allow better management of the available space inside the aluminum smelter.
• electrical conductors of superconducting material require less important support structures and therefore less expensive.
• the arrangement of the electrical conductor of superconducting material of the electrical circuit, wholly or partly, inside a magnetic shield enclosure has the advantage of preventing the electrical conductor of superconducting material from generating a surrounding magnetic field.
• this makes it possible to create passage zones for vehicles or vehicles whose operation would be disturbed by the intensity of the magnetic field at these areas of passage in the absence of magnetic shield. It also avoids the use of expensive gear with shielding protecting them from strong magnetic fields. This also allows stabilization of the electrolytic cells by locally controlling and adjusting the magnetic fields. It results from the use of such magnetic shield speakers the possibility of reducing the length of the conductors and their bulk.
• the magnetic shield enclosure may also be formed of superconducting material.
• Superconducting materials form high-performance magnetic screens when kept below their critical temperature.
• the electrical conductor of superconducting material is formed by a cable comprising a central core made of copper or aluminum, at least one fiber of superconducting material and a cryogenic envelope.
• the cryogenic envelope is traversed by a cooling fluid.
• the cooling fluid is liquid nitrogen and / or helium.
• the magnetic shield enclosure is made of superconductive material and is disposed inside the cryogenic envelope of the cable forming the electrical conductor of superconducting material.
• This enclosure is thus as close as possible to the electrical conductors made of superconductive material, so that the mass of superconducting material of the enclosure is minimized and the superconducting material of the enclosure is kept below its critical temperature without it being necessary. to have another specific cooling system.
• said electrical conductor of superconducting material extends over a length equal to or greater than ten meters.
• an electrical conductor of superconducting material is particularly advantageous when it has a certain length, especially greater than or equal to ten meters .
• the electrical conductor of superconducting material of the secondary electrical circuit is flexible and has at least one curved portion.
• the secondary electrical circuit may comprise one or more non-rectilinear portions (s).
• the flexibility of the electrical conductor in superconducting material makes it possible to avoid obstacles (thus to adapt to the spatial constraints of the aluminum smelter), but also to refine the compensation of the magnetic field locally.
• the magnetic shield enclosure is located at at least one end of the electrolysis cell line (s).
• the latter further comprises at least one secondary electric circuit, intended to be traversed by a current, along the line or rows of electrolysis cells, said electrical conductor material superconductor part of the secondary electrical circuit and being placed partly inside the magnetic shield enclosure.
• the magnetic field generated by the secondary electrical circuit is not beneficial over its entire length and it may be particularly advantageous to attenuate or cancel the effects on certain portions. This is particularly the case at the ends of the row or rows of electrolysis tanks, to improve the stability of the end tanks of the line, to allow the passage of vehicles whose operation would be disturbed by the intensity of the field magnetic or to limit the distance conventionally necessary, and therefore the length, of the electrical conductors arranged at the ends of queues.
• the electrical conductor of superconducting material of the secondary electrical circuit runs at least twice the row or rows of electrolytic cells, so as to perform several turns in series.
• the loop formed by the secondary electrical circuit thus runs several times the row or rows of tanks, and includes several rounds in series. This makes it possible to divide by the number of turns the value of the intensity of the current flowing through the electrical conductor in superconductive material, and consequently to reduce the cost of the power supply station intended to deliver this current to the secondary electrical circuit and the cost of the junctions between the poles of the power station and the electrical conductor of superconducting material.
• the electrical conductor of superconductive material of the secondary electrical circuit comprises a single cryogenic envelope, inside which pass side by side the turns made by said electrical conductor of superconducting material.
• a single cryogenic envelope inside which pass side by side the turns made by said electrical conductor of superconducting material.
• the secondary electrical circuit comprises two ends, each end of said secondary electrical circuit being connected to an electrical pole of a feed station distinct from the feed station of the main circuit.
• the electrical conductor made of superconducting material of the secondary electrical circuit runs along the electrolysis cell line or queues a predetermined number of times in order to allow the use of a feed station of the secondary electrical circuit delivering a current of intensity. between 5 kA and 40 kA.
• the electrical conductor superconducting material thus performs as many rounds in series as necessary to allow the use of a power station that can be easily found in the trade and economically interesting.
• At least a portion of the electrical conductor of superconducting material of the secondary electrical circuit is disposed under or along the right side and / or the left side of the electrolytic cells of the or files.
• the main electrical circuit comprises at least one electrical conductor of superconducting material placed wholly or partly inside the magnetic shield enclosure.
• the series of electrolytic cells comprises at least two rows of electrolytic cells and the electrical conductor of superconducting material of the main electrical circuit placed wholly or partly inside the magnetic shield enclosure connects two rows of electrolytic cells. electrolysis tanks.
• the main electric circuit comprises two electrical conductors each connecting one pole of the supply station of said main electrical circuit to one end of the series of electrolysis cells and at least one two electrical conductors connecting a pole of the feed station to one end of the series of electrolysis cells is made of superconducting material and placed wholly or partly within the magnetic shield enclosure.
• the series of electrolysis cells comprises a single line and the electrical conductor of superconducting material of the main electrical circuit placed wholly or partly inside the enclosure forming Magnetic shield connects an end of the line to a pole of the power station of said main electrical circuit.
• FIG. 1 is a schematic view from above of an electrolysis cell belonging to the state of the technique
• FIG. 2 is a side view of an electrolysis cell of the state of the art
• FIGS. 3, 4, 5, 6 and 7 are schematic top views of an aluminum smelter, in which at least one electrical conductor of superconductive material is used in a secondary electrical circuit,
• FIGS. 8 and 9 are schematic top views of an aluminum smelter, in which an electrical conductor of superconducting material is used in the main electrical circuit,
• FIG. 10 is a partial schematic view from above of an aluminum smelter, in which it includes a secondary electrical circuit provided with a curved portion,
• FIG. 1 1 is a sectional view of an electrolysis cell of an aluminum smelter, having a particular positioning of the electrical conductors of superconducting material of two secondary electrical circuits, and also having the positioning that should have been used with conventional electrical conductors made of aluminum or copper,
• FIG. 12 is a schematic top view of an aluminum smelter with a single tank line,
• FIG. 13 is a schematic top view of an aluminum smelter with a single row of tanks.
• Figure 2 shows a typical example of electrolysis tank 2.
• the electrolysis tank 2 comprises in particular a metal box 3, for example made of steel.
• the metal casing 3 is lined internally with refractory and / or insulating materials, for example bricks.
• the electrolysis cell 2 also comprises a cathode 6 made of carbonaceous material and a plurality of anodes 7, intended to be consumed as the electrolysis reaction takes place in an electrolytic bath including cryolite and electrolysis. alumina.
• a blanket of alumina and milled bath generally covers the electrolytic bath and at least partially the anodes 7.
• a sheet of liquid aluminum is formed.
• the cathode 6 is electrically connected to cathode outlets 9 in the form of metal bars passing through the caisson 3, the cathode outlets 9 being themselves connected to electrical conductors 11 of tank to tank.
• the electric tank 11 conductors allow the flow of the electrolysis stream 11 from one electrolysis tank 2 to another.
• the electrolysis current 11 passes through the conductive elements of each electrolysis cell 2: firstly an anode 7, then the electrolytic bath 8, the liquid aluminum ply 10, the cathode 6 and finally the electrical conductors 1 1 of vat tub connected to the cathode outlets 9, to then convey the electrolysis current 11 to an anode 7 of the next electrolysis tank 2.
• the electrolysis tanks 2 of an aluminum plant 1 are conventionally arranged and electrically connected in series.
• a series may comprise one or more rows F of electrolysis tanks 2.
• the series comprises several rows F, they are generally rectilinear and parallel to each other, and are advantageously even in number.
• the aluminum smelter 1 an example of which is visible in FIG. 3, comprises a main electrical circuit 15 traversed by an electrolysis current 11.
• the intensity of the electrolysis current M can reach values of the order of several hundred thousands of amperes, for example of the order of 300 kA to 600 kA.
• a feed station 12 feeds the series of electrolysis tanks 2 electrolysis current 11.
• the ends of the series of electrolysis tanks 2 are each connected to an electrical pole of the feed station 12.
• Conductors 13 electric link connect the electrical poles of the power station 12 to the ends of the series.
• the rows F of a series are connected electrically in series.
• One or more electrical connecting conductors 14 allow the flow of the electrolysis current 11 from the last electrolytic cell 2 of a line F to the first electrolytic cell 2 of the following queue F to be conveyed.
• the main electrical circuit 15 consists of the electrical connecting conductors 13 connecting the ends of the series of electrolysis tanks 2 to the supply station 12, electric connecting conductors 14 connecting the rows F of the electrolysis tanks 2. to each other, electrical conductors 11 of the bottom of the tank connecting two electrolytic cells 2 of the same file F, and conductive elements of each electrolysis tank 2.
• the aluminum smelter 1 according to one embodiment of the present invention also comprises one or more secondary electrical circuits 16, 17, visible for example in FIG. 3. These secondary electrical circuits 16, 17 typically follow the lines F of tanks 2 of electrolysis. They make it possible to compensate for the magnetic field generated by the high value of the intensity of the electrolysis current 11, causing the instability of the electrolytic bath 8 and thus affecting the efficiency of the electrolysis tanks 2.
• Each secondary electrical circuit 16, 17 is traversed respectively by a current 12, 13, delivered by a feed station 18.
• the feed station 18 of each secondary circuit 16, 17 is distinct from the feed station 12 of the main circuit 15.
• the aluminum plant 1 comprises one or more electrical conductors of superconducting material.
• These superconducting materials may for example comprise BiSrCaCuO, YaBaCuO, MgB2, materials known from patent applications WO2008011184, US20090247412 or other materials known for their superconducting properties.
• Superconducting materials are used to carry current with little or no Joule heat generation loss because their resistivity is zero when held below their critical temperature. Because of this absence of energy loss, it is possible to devote a maximum of the energy received by the aluminum smelter (for example 600kA and 2kV) to the main electrical circuit 15 which produces aluminum, and in particular to increase the number of vats 2.
• a superconducting cable used to implement the present invention comprises a central core made of copper or aluminum, ribbons or fibers of superconducting material, and a cryogenic envelope.
• the cryogenic envelope may be formed by a sheath containing a cooling fluid, for example liquid nitrogen.
• the cooling fluid makes it possible to maintain the temperature of the superconducting materials at a temperature below their critical temperature, for example less than 100 K (Kelvin), or between 4 K and 80 K.
• the electrical conductors of superconducting material are particularly advantageous when they have a certain length, and more particularly a length equal to or greater than 10 m. .
• Figures 3, 4 and 5 illustrate, by way of non-exhaustive examples, various possible embodiments of an aluminum smelter 1.
• the electrical conductors of superconducting material are represented by dashed lines in the various figures.
• the example of Figure 3 shows an aluminum smelter 1 comprising two secondary electrical circuits 16 and 17, respectively traversed by intensity currents 12 and 13 and each supplied by a feed station 18.
• the currents 12 and 13 travel through the respective secondary electric circuits 16 and 17 in the same direction as the electrolysis current 11.
• the secondary electrical circuits 16 and 17 in this case provide compensation for the magnetic field generated by the electric conductors 11. from tank to tank.
• the intensity of each of the electric currents 12, 13 is important, for example between 20% and 100% of the intensity of the electrolysis current 11 and preferably from 40% to 70%.
• the compensation of the magnetic field of the neighboring queue F can be obtained with the example of FIG. 4.
• the aluminum plant 1 illustrated in FIG. 4 comprises a secondary electrical circuit 17 forming an internal loop, traversed by an electric current 13.
• the use of electrical conductors of superconducting material to form the secondary circuit or circuits 16, 17 is interesting because of the length, of the order of two kilometers, of the secondary electrical circuits 16, 17.
• the use of electrical conductors in superconducting material requires less voltage compared to that required by electrical conductors made of aluminum or copper.
• the cost of the station 18 for supplying the secondary electrical circuit or circuits is reduced accordingly.
• the aluminum smelter 1 may comprise a secondary electrical circuit 16, 17 provided with an electrical conductor made of superconducting material and running substantially at the same place, advantageously at least twice, the same row F of the electrolysis tanks 2 so as to carry out several turns in series, as is particularly visible in Figures 6 and 7.
• the small size of the electrical conductors of superconducting material relative to electrical conductors made of aluminum or copper facilitates several series turns in the loops formed by the secondary electrical circuits 16, 17.
• the aluminum smelter 1 according to the embodiment illustrated in FIG. 6 comprises a secondary electrical circuit 16, the electrical conductors of which line the series F of the series twice in series.
• the aluminum smelter 1 comprises a secondary electrical circuit 16 along both the left side and the right side of the electrolysis tanks 2 of the series (left side and right side being defined by compared to an observer placed at the level of the main electrical circuit 15 and directing his gaze in the direction of global circulation of the electrolysis current 11).
• the electrical conductors (made of superconducting material) of the secondary electrical circuit 16 of the aluminum smelter 1 shown in FIG. 7 carry out several turns in series, including two laps along the left sides of the tanks 2 of the series and three turns in along the right sides. The number of turns could be twenty and thirty respectively.
• This cryogenic envelope may comprise a thermally insulated sheath in which a cooling fluid circulates. At a given location, the cryogenic envelope can therefore contain side by side several passages of the same electrical conductor of superconducting material. This would be more restrictive with aluminum or copper electrical conductors making several turns around the series of electrolysis tanks. Electrical conductors made of aluminum or copper are indeed more bulky than electrical conductors of superconducting material.
• the aluminum smelter 1 may thus comprise one or more secondary electrical circuits 16, 17 comprising an electrical conductor of superconducting material having at least one curved portion. This makes it possible to bypass the obstacles 19 present inside the aluminum smelter 1, for example a pillar, as can be seen in FIG.
• This also makes it possible to locally adjust the compensation of the magnetic field in the smelter 1 by locally adjusting the position of the electrical conductor in superconducting material of the secondary electrical circuit or circuits 16, 17, as allowed by the curved portion 16a of the secondary electrical circuit 16 of the aluminum smelter 1 visible in FIG. 10.
• This flexibility makes it possible to move the electrical conductor in superconducting material with respect to its initial position, to correct the magnetic field by adapting to the evolution of the smelter 1 (for example increasing the intensity of the electrolysis current 11, or to use the results of the most recent magnetic correction calculations that are enabled by the new computer powers and general knowledge on the subject).
• the electrical conductors of superconducting material or secondary electrical circuits 16, 17 may be arranged under the electrolysis tanks 2. In particular, they can be buried. This arrangement is made possible by the small size of the electrical conductors of superconducting material on the one hand, and by the fact that they do not heat on the other hand. This provision would be difficult to achieve with electrical conductors made of aluminum or copper, because their size is greater at equal intensity, and because they heat and therefore need to be cooled (commonly in contact with the air and / or with specific cooling means).
• FIG. 11 shows, for the same aluminum plant 1, the possible locations of secondary electric circuits 16, 17 with electrical conductors of superconducting material and of secondary electrical circuits 16 ', 17' using aluminum electrical conductors.
• the secondary electrical circuits 16 ', 17' are placed on either side of an electrolysis cell 2. As illustrated in FIG. 11, the secondary electrical circuits 16 ', 17' prevent access to the electrolysis tanks 2, for example for maintenance operations. However, they can not be placed under the electrolysis tanks 2, such as the secondary electrical circuits 16, 17 with electrical conductors of superconducting material, because they have a larger footprint and need to be cooled. The secondary electrical circuits 16, 17 using electrical conductors of superconducting material may, however, be placed under the electrolysis tanks 2. Access to the electrolysis tanks 2 is thus not limited.
• the electrical conductors made of superconductive material may be contained partly inside a magnetic shield enclosure 20.
• This enclosure 20 may be a metal tube, for example steel. It can significantly reduce the magnetic field outside of this magnetic shield. This thus makes it possible to create, in the places where this chamber 20 has been placed, passage zones, in particular of vehicles the operation of which would have been disturbed by the magnetic field emanating from the electrical conductors made of superconducting material. This makes it possible to reduce the cost of these vehicles (which must otherwise be equipped with protection).
• This enclosure 20 may advantageously be placed around the electrical conductors of superconducting material located at the end of the line F, as shown in FIG. 6.
• a protective enclosure 20 is not possible with conventional electrical conductors of the prior art made of aluminum or even copper. These aluminum electrical conductors actually have a section of significant dimensions, of the order of 1 m by 1 m, against 25 cm in diameter for an electrical conductor of superconducting material. Above all, aluminum electrical conductors heat up in operation. The use of such a magnetic shield enclosure 20 would not allow a proper evacuation of the heat generated.
• the magnetic shield enclosure 20 may also be formed of superconducting material maintained below its critical temperature. Superconducting materials form high-performance magnetic screens when kept below their critical temperature.
• this enclosure of superconductive material forming a magnetic shield may be disposed inside the cryogenic envelope of the cable forming the electrical conductor of superconducting material. The enclosure 20 is thus as close as possible to the electrical conductors of superconducting material and the mass of superconducting material of the enclosure is minimized and the superconducting material of the enclosure is kept below its critical temperature without it being necessary to have another specific cooling system.
• the magnetic shield enclosure made of superconductive material may be made independently of the cable forming the electrical conductor made of superconducting material, around this cable. This is particularly the case when such an enclosure must be installed around an electrical conductor made of superconducting material already installed.
• the magnetic shield enclosure made of superconducting material then has its own cooling system.
• the electrical conductors of superconducting material have a mass per meter which can be twenty times lower than that of an aluminum electrical conductor for an equivalent intensity.
• the cost of the supports of the electrical conductors in superconducting material is therefore lower and their installation is facilitated.
• the main electrical circuit 15 of the aluminum smelter 1 may also comprise one or more electrical conductors of superconducting material.
• the electrical connecting conductors 14 electrically connecting the rows F of the series to each other may be of superconducting material, as shown in FIG. 8.
• the electrical connecting conductors 13, connecting the ends of the series of cells 2 Electrolysis at the poles of the feed station 12 of the main circuit 15 may also be of superconducting material, as shown in FIG. 9.
• the electrical connecting conductors 14 connecting two rows F measure from 30m to 150m depending on whether the two lines F they connect are in the same building or in two separate buildings for reasons of magnetic interaction between them.
• two lines F The electrical connecting leads 13 connecting the ends of the series to the poles of the power station 12 generally measure from 20m to 1 km depending on the positioning of this station 12 supply. Because of these lengths and the intensity of the electrical current flowing through these conductors, it will be understood that the use of electrical conductors of superconducting material at these locations can achieve energy savings. The weak The size of such conductors of superconducting material is furthermore appreciated.
• the use of electrical connection conductors 14 and / or 13 made of superconducting material makes it possible, according to one embodiment of the invention, to place them inside a shield enclosure 20.
• magnetic This makes it possible to create passage zones for vehicles or vehicles at the ends of the line. This allows above all a stabilization of the electrolytic cells by canceling, controlling and / or adjusting locally the magnetic fields generated by these electrical connecting conductors.
• As a result of the use of such magnetic shield enclosures 20 around the electrical connection conductors at the end of the line the possibility of reducing the length of the conductors and their bulk.
• the electrical connecting conductors connecting the ends of two rows have a U-shape with the two elongate branches, several tens of meters, so that the magnetic field generated by the seat U n ' It does not affect the magnetic stability and the operation of the tanks arranged at the end of the line too much.
• Such a distance from this seat of the U generates a significant cost of the driver, an important cost of the building and a loss of productivity for a given surface.
• the fact of being able to place such electrical connection conductors inside magnetic shield enclosures makes it possible to reduce the length of these branches of the U because the magnetic field generated by the U-shaped base is no longer detrimental to the operation. end-of-line tanks.
• the aluminum smelter 1 may also comprise a single file F of electrolysis tanks 2, as shown in FIG. 12 and FIG. 13. This is the case, for example, of an aluminum smelter 1 under construction with a production started while half of the electrolysis tanks 2 was built. This can also be the case when the available space does not offer the possibility of setting up several rows F of electrolysis tanks 2.
• the end of the row F of electrolysis tanks 2 is electrically connected to the electrolysis current supply station 12 by the electrical conductor 13 which is made of superconducting material.
• a magnetic shield enclosure 20 surrounds the electrical conductor 13 in order to protect the single file F from the effects of the magnetic field generated by the passage of the electrolysis current 11 in the electrical conductor 13.
• the aluminum plant 1 comprises a single tank line F
• This file F electrolysis tanks 2 is traversed by an electrolysis current 11 of high intensity.
• the main electrical circuit 15 At the end of the tank line F 2 opposite the end of the line F connected to the supply station 12, the main electrical circuit 15 has a node and the electrical circuit separates into two circuits with each its intensity.
• the electrical conductors carrying the current (of intensity equal to half that of the electrolysis current 11) from the node to the supply station 12 are made of superconducting material. These electrical conductors made of superconducting material may repeatedly run along one side of the line F of electrolysis tanks 2 (three times in the example of FIG. 13).
• these electrical conductors of superconducting material are contained in a chamber 20 forming a magnetic shield.
• these electrical conductors of superconducting material are not contained in a chamber 20 forming a magnetic shield. They thus make it possible to generate a magnetic field that compensates for the undesirable effects of the magnetic field generated by the circulation of the electrolysis current 11 in the line F of electrolysis tanks 2 on the liquids contained in the electrolysis tanks 2.
• the use of electrical conductors of superconducting material in an aluminum smelter 1 may be advantageous for sufficiently high conductor lengths.
• the use of electrical conductive material conductors is particularly advantageous for secondary electrical circuits 16, 17 for reducing the effect of the tank-to-cell magnetic field by means of loops of the type described in patent document EP0204647; when the intensity of the current flowing in the main electrical circuit 15 is particularly high, greater than 350 kA, and when the sum of the intensities flowing in the secondary electrical circuit, in the same direction as the current flowing in the main circuit, is between 20% and 100% of the main circuit current, and preferably 40% to 70%.
• a main electrical circuit 15 comprising both an electrical conductor 14 for connecting a file to a file of superconducting material disposed at inside a magnetic shield enclosure, electrical connecting leads 13 connecting the ends of a series to the poles of the superconducting material supply station 12 disposed within magnetic shield enclosures, and a or a plurality of secondary electrical circuits 16, 17 also comprising electrical conductors of superconducting material producing several series turns arranged in part inside magnetic shield enclosures.
• the invention can be extended to aluminum smelters with electrolysis with inert anodes.

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• Chemical & Material Sciences (AREA)
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• Electrochemistry (AREA)
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• Organic Chemistry (AREA)
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• 2012
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