Aluminium Smelter Comprising a Compensating Electric Circuit

Patent metadata

Field	Value
Publication number	US-2016201208-A1
Application number	US-201414911099-A
Country	US
Kind code	A1
Filing date	Jul 30, 2014
Priority date	Aug 9, 2013
Publication date	Jul 14, 2016
Grant date	—

Abstract

This aluminum smelter comprises a row of cells ( 50 ) arranged transversely in relation to the length of the row, the cells ( 50 ) individually comprising an anode ( 52 ), rising and connecting electrical conductors ( 54 ) running upwards along the two opposite longitudinal edges of the cell ( 50 ) to route the electrolysis current towards the anode ( 52 ), and a cathode ( 56 ) through which pass cathode conductors ( 55 ) connected to cathode outputs connected to linking conductors to route the electrolysis current to the rising and connecting electrical conductors of the next cell ( 50 ). Furthermore the aluminum smelter comprises a compensating electrical circuit separate from the electrical circuit through which the electrolysis current flows, running beneath the cells ( 50 ), through which a compensating current may flow beneath the cells ( 50 ) in a direction opposite to the overall direction of flow of the electrolysis current.

First claim

1 . An aluminum smelter comprising at least one row of electrolytic cells arranged transversely in relation to a length of the at least one row, each of the electrolytic cells comprising a pot shell, anode assemblies each comprising a support and at least one anode, and a cathode through which pass cathode conductors intended to collect an electrolysis current at the cathode to route the electrolysis current to cathode outputs outside the pot shell, characterized in that each electrolytic cell comprises rising and connecting electrical conductors to the anode assemblies running upwards along two opposite longitudinal edges of the electrolytic cell to conduct the electrolysis current to the anode assemblies, and linking conductors connected to the cathode outputs designed to route the electrolysis current from the cathode outputs to electrical rising and connecting conductors of the next electrolytic cell, and in that the aluminum smelter comprises at least one electrical compensating circuit running beneath the electrolytic cells, through which compensating circuit may flow a compensating current flowing beneath the electrolytic cells in a direction opposite to an overall direction of flow of the electrolysis current passing through the electrolytic cells located above.

2 . Aluminum smelter according to claim 1 , in which the compensating electrical circuit is a secondary compensating electrical circuit separate from the electrical circuit through which the electrolysis current flows.

3 . Aluminum smelter according to claim 1 , characterized in that the aluminum smelter comprises two rows of cells arranged parallel to each other, supplied from a single station and electrically connected in series in such a way that the electrolysis current flowing in a first of the two rows of cells then flows in a second of the two rows of cells in a direction which is overall opposite to that in which the electrolysis current flows in the first of the two rows, and in that the compensating electrical circuit forms a loop beneath the two rows of parallel cells.

4 . Aluminum smelter according claim 1 , characterized in that the electrolytic cell comprises a plurality of rising and connecting electrical conductors distributed at predetermined intervals over substantially an entire length of the corresponding longitudinal edge along each of two longitudinal sides of the electrolytic cell.

5 . Aluminum smelter according to claim 1 , characterized in that the rising and connecting electrical conductors are arranged in a substantially symmetrical way in relation to a longitudinal median plane of the electrolytic cell.

6 . Aluminum smelter according to claim 1 , characterized in that the linking conductors run substantially straight beneath the electrolytic cell in a transverse direction in relation to the electrolytic cell.

7 . Aluminum smelter according to claim 1 , characterized in that the compensating electrical circuit comprises electrical conductors forming a plurality of secondary compensating electrical sub-circuits which are independent of each other.

8 . Aluminum smelter according to claim 1 , characterized in that the compensating electrical circuit comprises electrical conductors running in parallel beneath the electrolytic cells.

9 . Aluminum smelter according to claim 1 , characterized in that electrical conductors forming the compensating electrical circuit run beneath the electrolytic cells, together forming a layer of between two and twelve parallel electrical conductors.

10 . Aluminum smelter according to claim 7 , in which the electrical conductors are substantially equally spaced and are arranged substantially symmetrically in relation to a transverse median axis of the electrolytic cells.

11 . Aluminum smelter according to claim 1 , characterized in that the rising and connecting electrical conductors running along one of the two longitudinal edges of the electrolytic cell are in a staggered arrangement in relation to the rising and connecting electrical conductors located on an adjacent longitudinal edge of a separate preceding or following electrolytic cell.

12 . Aluminum smelter according to claim 1 , characterized in that each cathode output eaves the pot shell only in a vertical plane perpendicular to a longitudinal direction of the electrolytic cell.

13 . Aluminum smelter according to claim 1 , characterized in that the support for each anode assembly comprises a cross-member extending transversely in relation to the electrolytic cell, being supported and electrically connected at each of the two longitudinal edges on either side of the electrolytic cell.

14 . Aluminum smelter according to claim 1 , characterized in that the rising and connecting conductors run on either side of the pot shell, without running above the at least one anode.

15 . Aluminum smelter according to claim 1 , characterized in that the rising and connecting electrical conductors run at a height of between 0 and 1.5 metres above a substantially horizontal plane, including a surface of liquids present in the electrolytic cell.

16 . Method for using an aluminum smelter according to claim 1 , comprising passing the compensating current through the compensating circuit beneath the electrolysis cells ( 50 ) in the direction opposite to the overall direction of flow of the electrolysis current flowing through the electrolytic cells located above.

17 . Method according to claim 16 , characterized in that an intensity of the compensating current is of the order of 50% to 150% of an intensity of the electrolysis current.

18 . Method according to claim 17 , characterized in that the intensity of the compensating current is of the order of 70% to 130% of the intensity of the electrolysis current.

19 . Method according to claim 16 , characterized in that a distribution of current between the rising and connecting electrical conductors located upstream of the electrolytic cell and the rising and connecting electrical conductors located downstream of the electrolytic cell is of the order of 30-70% upstream and 30-70% downstream respectively.

20 . Method according to claim 19 , characterized in that the distribution of current between the rising and connecting electrical conductors located upstream of the electrolytic cell and the rising and connecting electrical conductors located downstream of the electrolytic cell is of the order of 40-60% upstream and 40-60% downstream respectively.

21 . Method according to claim 20 , characterized in that the distribution of current between the rising and connecting electrical conductors located upstream of the electrolytic cell and the rising and connecting electrical conductors located downstream of the electrolytic cell is of the order of 45-55% upstream and 45-55% downstream respectively.

22 . Process for stirring fee-alumina present in the electrolytic cells of an aluminum smelter according to claim 1 , the process comprising:
analyzing of at least one characteristic of the alumina, determining an intensity value for an intensity of the compensating current which has to flow in the compensating electrical circuit as a function of the at least one characteristic analyzed, changing the intensity of the compensating current to the intensity value determined, if the intensity of the compensating current differs from the intensity value.

Assignees

• Rio Tinto Alcan Int Ltd

Inventors

• Renaudier Steeve
• BARDET Benoit
• Martin Olivier
• Duval Christian

Classifications

• C25C3/24

  Refining · CPC title

• C25C3/16 Primary

  Electric current supply devices, e.g. bus bars · CPC title

• C25C7/005

  of cells for the electrolysis of melts (C25C7/02 - C25C7/06 take precedence) · CPC title

• C25C3/20 Primary

  Automatic control or regulation of cells (controlling or regulating in general G05) · CPC title