EP3571333B1 - Cathode assembly with metallic collector bar for electrolytic cell suitable for the hall-héroult process - Google Patents
Cathode assembly with metallic collector bar for electrolytic cell suitable for the hall-héroult process Download PDFInfo
- Publication number
- EP3571333B1 EP3571333B1 EP18741304.2A EP18741304A EP3571333B1 EP 3571333 B1 EP3571333 B1 EP 3571333B1 EP 18741304 A EP18741304 A EP 18741304A EP 3571333 B1 EP3571333 B1 EP 3571333B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- bar
- slot
- cathode
- side wall
- wall
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000009626 Hall-Héroult process Methods 0.000 title claims description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 31
- 230000000712 assembly Effects 0.000 claims description 21
- 238000000429 assembly Methods 0.000 claims description 21
- 238000000034 method Methods 0.000 claims description 19
- 230000008569 process Effects 0.000 claims description 19
- 229910002804 graphite Inorganic materials 0.000 claims description 18
- 239000010439 graphite Substances 0.000 claims description 18
- 239000011888 foil Substances 0.000 claims description 17
- 238000003466 welding Methods 0.000 claims description 16
- 238000005520 cutting process Methods 0.000 claims description 14
- 238000005868 electrolysis reaction Methods 0.000 claims description 14
- 239000004411 aluminium Substances 0.000 claims description 13
- 229910052782 aluminium Inorganic materials 0.000 claims description 13
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 11
- 239000003575 carbonaceous material Substances 0.000 claims description 8
- 239000007769 metal material Substances 0.000 claims description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 22
- 229910052802 copper Inorganic materials 0.000 description 22
- 239000010949 copper Substances 0.000 description 22
- 229910000831 Steel Inorganic materials 0.000 description 12
- 229910052799 carbon Inorganic materials 0.000 description 12
- 238000003780 insertion Methods 0.000 description 12
- 230000037431 insertion Effects 0.000 description 12
- 239000010959 steel Substances 0.000 description 12
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 6
- 239000011244 liquid electrolyte Substances 0.000 description 5
- 238000003754 machining Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000003292 glue Substances 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910001610 cryolite Inorganic materials 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 229910001338 liquidmetal Inorganic materials 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000010406 cathode material Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000007770 graphite material Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- -1 oxygen ions Chemical class 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000007514 turning Methods 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
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
- 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
Definitions
- the invention relates to the field of fused salt electrolysis using the Hall-Heroult process for making aluminium. More specifically it relates to the improvement of the cathode blocks of such an electrolysis cell, the improvement being related to the cathode drop and the current distribution along the cathode blocks. In particular, the invention relates to an improvement for cathode block provided with a cathode collector bar.
- the Hall-Héroult process is the only continuous industrial process for producing metallic aluminium from aluminium oxide.
- Aluminium oxide Al 2 O 3
- molten cryolite Na 3 AlF 6
- the resulting mixture typically at a temperature comprised between 940 °C and 970 °C acts as a liquid electrolyte in an electrolytic cell.
- An electrolytic cell used for the Hall-Heroult process typically comprises a steel shell (so-called pot shell), a lining (comprising refractory bricks protecting said steel shell against heat, and cathode blocks usually made from graphite, anthracite or a mixture of both), and a plurality of anodes (usually made from carbon) that plunge into the liquid electrolyte contained in the volume defined by the cathode bottom and a side lining made from carbonaceous material.
- Anodes and cathodes are connected to external busbars.
- An electrical current is passed through the cell (typically at a voltage between 3.5 V and 5 V) which electrochemically reduces the aluminium oxide, split in the electrolyte into aluminium and oxygen ions, then into aluminium at the cathode and oxygen at the anode; said oxygen reacting with the carbon of the anode to form carbon dioxide.
- the resulting metallic aluminium is not miscible with the liquid electrolyte, has a higher density than the liquid electrolyte and will thus accumulate as a liquid metal pad on the cathode surface below the electrolyte from where it needs to be removed from time to time, usually by suction into a crucible.
- Industrial electrolytic cells used for the Hall-Heroult process are generally rectangular in shape and connected electrically in series, the ends of the series being connected to the positive and negative poles of an electrical rectification and control substation.
- the general outline of these cells is known to a person skilled in the art and will not be repeated here in detail. They have a length usually comprised between 8 and 25 meters and a width usually comprised between 3 and 5 meters.
- the cells also called “pots” are always operated in series of several tens (up to several hundreds) of pots (such a series being also called a "potline”); within each series DC currents flow from one cell to the neighbouring cell.
- the electrical currents in most modern electrolytic cells using the Hall-Héroult process exceed 200 kA and can reach 400 kA, 450 kA or even more; in these potlines the pots are arranged side by side. Most newly installed pots operate at a current comprised between about 350 kA and 600 kA, and more often in the order of 400 kA to 500 kA. The passage of these enormous current intensities through the electrolytic cell leads to ohmic losses at various locations of the pot and its environment.
- Cathode assemblies for use in electrolytic cells suitable for the Hall-Heroult process are industrially manufactured for more than a century, and the state of the art is summarized in the reference book " Cathodes in Aluminium Electrolysis” by M. S ⁇ rlie and H. ⁇ ye, 3rd edition (Düsseldorf 2010 ). They comprise a cathode body made from a carbon material and one or more metallic cathode bars that are fitted into slots or grooves machined into the lower surface of said carbon body. Said metallic cathode bar protrudes out of each end of the cathode block, thereby allowing to connect the cathode assembly to the cathode busbar system.
- the metallic cathode bar is usually mode from steel; copper inserts within the steel bar can be used in order to increase the electrical conductivity of the cathode bar.
- Said steel bars are inserted into grooves that are wider than the steel bars, and then fixed with electrically conductive glue (carbonaceous glue or cement, or ramming paste) or with cast iron that is poured into the interstitial space between the steel bar and the carbon body, as described in GB 663 763 (assigned to Compagnie de Produits Chimiques et Electrométallurgiques Alais, Froges & Camargue).
- a cathode with a full copper cathode bar inlaid into a groove machined in the lower surface of the carbon body is known from WO 2016/079605 (Kan Nak s.a.), in particular figures 7 and 9 of said document.
- the contact between the carbon body and the copper bar is critical for the electrical performance of the electrolysis cell. Copper has a much higher thermal expansion coefficient than the carbon material of the cathode block body, and the copper bar in direct contact with the carbon body will operate at a temperature that is probably less than 100°C lower than its melting point, leading to significant thermal expansion. As a consequence, a well-defined allowance for thermal expansion must be groove is required in order to ensure a good and reliable electrical contact between the copper bar and the carbon body over the whole length.
- Reliability of this contact is of paramount importance, because once installed into a cell and the cell started, a cathode block cannot be repaired, and cannot be replaced without relining of the whole cell.
- the normal lifetime of a cathode lining is comprised between five and seven years.
- the problem addressed by the present invention is therefore to improve the quality and reliability of the electrical contact of metallic bars, in particular copper bars, inserted into grooves machined into the carbon body of a cathode block.
- a first object of the invention is a cathode assembly suitable for a Hall-Heroult electrolysis cell, comprising
- said cathode assembly is provided with fixation means, in particular permanent fixation means, between said tapered walls of said bar elements.
- fixation means are advantageously welding means.
- said welding means comprise at least one welding line, in particular several welding lines, extending over at least part of said contact line.
- said cathode body is provided with at least one first and one second slots, each slot being provided with a blind wall defining a longitudinal end of said slot, each slot receiving a respective cathode bar.
- said cathode bar is jammed against said longitudinal end of a respective slot.
- one first bar element has a triangular shape and comprises a front wall, said main side wall and said tapered wall.
- one second bar element comprises a further side wall, opposite to main side wall, said further side wall protruding with respect to main side wall of first bar element, along a transversal direction of said slot.
- said front wall of first bar element is positioned against longitudinal end of said slot, and said second bar element comprises a front wall, the length of which is far inferior to that of front wall of first bar element, front wall of second bar element being remote from end of said slot.
- said cathode bar has two portions, i.e. a first portion the width of which is equal to that of slot, as well as a second portion the width of which is superior to that of slot.
- said cathode bar has a protrusion which extends outside said slot.
- Said protrusion is in particular formed by said second portion and by a fraction of said first portion.
- main side wall of each bar element protrudes outside said slot.
- main side wall of each bar element directly contacts a respective side wall of said slot.
- main side wall of each bar element indirectly contacts a respective side wall of said slot, an intercalary material, in particular at least one graphite foil, being interposed between said main side wall and said respective side wall of said slot.
- an intercalary material in particular at least one further graphite foil, may be interposed between upper wall of said slot and facing walls of bar elements.
- said side walls of said slot and said side walls of said bar elements show a slope, the value of which is in particular of about 10 degrees, so as to retain said bar elements in the inner volume of said slot.
- Said cathode bar is advantageously made of copper.
- said cathode bar is made of steel.
- Another object of the present invention is a process for making a cathode assembly as described above, comprising the steps of
- urging forward said second bar element also provokes the jamming of said first bar element against one longitudinal end of said slot.
- said process further comprises providing said side walls of said slot and said side walls of said bar elements with a slope, the value of which is in particular of about 10 degrees, so as to retain said bar elements in the inner volume of said slot.
- second bar element is provided with a handling portion and said second bar is urged forward manually, by handling said handling portion.
- bar elements are provided by cutting a rough bar along a cutting line, said cutting line being tapered with respect to main axis of said rough bar.
- said process further comprises providing fixation means, in particular permanent fixation means, between said tapered walls of said bar elements, once said tapered walls of said bar elements are in mutual contact.
- Another object of the present invention is an electrolytic cell suitable for the Hall-Heroult electrolysis process, comprising a cathode forming the bottom of said electrolytic cell and comprising a plurality of parallel cathode assembly, each cathode assembly comprising at least one metallic cathode collector bar protruding out of each of the two ends of the cathode, a lateral lining defining together with the cathode a volume containing the liquid electrolyte and the liquid metal resulting from the Hall-Heroult electrolysis process, an outer metallic potshell containing said cathode and lateral lining, a plurality of anode assemblies suspended above the cathode, each anode assembly comprising at least one anode and at least one metallic anode rod connected to an anode beam, a cathodic bus bar surrounding said potshell, said bus bar being connected to at least part of said cathode assemblies said electrolytic cell being characterized in that at least one of said cathode assembly, and preferably more than 60%
- Another object of the present invention is an electrolytic cell for the production of aluminium by the Hall-Heroult process, comprising at least one cathode assembly as described above.
- Another object of the present invention is a process for making aluminium by the Hall-Héroult process, using an electrolytic cell provided with cathode assemblies as described above.
- C Cathode assembly 1 Cathode body 11,12 Front/rear wall of cathode body 1 171, 172 Side walls of slot 17 13,14 Upper/lower wall of cathode body 1 173 Top wall of slot 17,17' 15,16 Side walls of cathode body 1 174,174' Blind wall of slot 17,17' 17, 17' Slots in cathode body 1 D174 Distance between 174 174' 3,3' Cathode bar 31,32 Front/rear wall of cathode bar 3 33,34 Side walls of cathode bar 3 37 Contact line of 3 5 Rough bar 51,52 Front / rear wall of rough bar 5 53,54 Upper / lower wall of rough bar 5 55,56 Side walls of rough bar 5 A5 Axis of rough bar 5 CL Cutting line L6 Length of slotted bar ⁇ s Angle of slotted bar ⁇ c Angle between A5 and CL A17,A17' Axis of slots 17, 17' 7, 9 Bar elements 9A Handling part of 9 9B Tip
- a cathode assembly comprises a cathode body 1 and at least one cathode bar 3 .
- the present invention is first applicable to cathode assemblies C comprising a cathode body 1 and at least one cathode bar 3 and 3'.
- the invention is applicable to cathode assemblies comprising two cathode bars 3 , 3' , one 3 of which is protruding out of the front wall 11 , the other 3' protruding out of the rear wall 12 of the cathode body 1.
- These cathode bars which are half bars, form two portions of a so-called "split bar” in the sense that they are not through bars, i.e. each cathode bar is not extending through the whole length of the cathode block.
- the present invention is also applicable to cathode assemblies having one (or more) through bar(s) instead of above defined split bars.
- the invention applies in particular to such through bars, which have a short length.
- split bars is preferred, since it allows a better jamming of these bars, as will appear at reading the following description.
- the present invention applies to cathodes used in the Hall-Heroult process that form the bottom of an electrolysis cell, said cathodes being assembled from individual cathode assemblies C , each of which bears at least one cathode bar 3 , 3'.
- the Hall-Heroult process and the outline of an electrolysis cell (also called “pot") are known to a person skilled in the art and will not be described here in great detail.
- the cathode assembly of the invention is designated as a whole by alphanumeric reference C. It is suitable for a Hall-Heroult electrolysis cell, but could be used in other electrolytic processes.
- the cathode assembly C first comprises a cathode body 1 , of known type, which is made of a carbonaceous material, typically graphitized carbon or graphite.
- This cathode body 1 which has an elongated shape, has opposite end walls, i.e. front 11 and rear 12 walls, as well as peripheral walls. The latter are formed by parallel upper and lower walls 13 and 14 , as well as parallel side walls 15 and 16.
- its length L1 (see figure 3 ), i.e. the distance between walls 11 and 12 , is between about 3100 millimetres (mm) and about 4000 mm.
- its width W1 see figure 2 ), i.e.
- the distance between walls 15 and 16 is between about 400 mm and about 700 mm.
- its height H1 (see figure 3 ) , i.e. the distance between walls 13 and 14 , is between about 375 mm and about580 mm.
- the lower wall 14 of cathode body 1 is provided with two housings, each being formed by a respective longitudinal slot 17 and 17' , the longitudinal main axis of which is referenced A17 , A17'.
- Figure 2 shows cathode body "upside down", with reference to its above defined industrial use position.
- Each slot 17 , 17' is provided with opposite side walls 171 , 171' and 172 , 172' (see figure 2 ), parallel to said main axis A17 , A17' , whereas its top wall is referenced 173 , 173' (see figure 3 ).
- each slot 17 , 17' is provided with a respective rear wall, or blind wall 174 , 174' (see figure 2 ), each defining a respective longitudinal end of said slot.
- the distance D174 (see figure 3 ) between these two walls is typically between 200 millimetres (mm) and 600 mm. Viewed from bottom, blind wall 174 , 174' is rounded, which makes it possible to ease the slot machining.
- First slot 17 does lead to front wall 11 of this cathode body, whereas second slot 17' does lead to rear wall 12 of this cathode body.
- width W17 or W17' (see figure 2 ) of each slot 17 , 17 ', i.e. the distance between side walls, is between about 50 mm and about 250 mm.
- each side wall 171 and 172 shows a slope, the value as of which is typically of about 10 degrees. Therefore the above defined width W17 or W17' decreases from top wall 173 , 173' of this slot to lower wall 14 of cathode body. As will be described hereafter, these slopes make it possible to maintain the bar elements in the inner volume of the slot, when turning over the cathode assemblies. For sake of clarity, the value of as is exaggerated on this figure 11 .
- depth D17 or D17' of each slot 17, 17' is between about 50 mm and about 150 mm.
- its length L17 or L17' is between about 1200 mm and about 1850 mm. This length is taken from the junction of rounded portion of said blind wall with rectilinear part of side walls 171 , 171' and 172, 172'.
- the cathode assembly C also comprises two cathode bars 3 and 3' (schematically shown on figure 1 ), each of which is accommodated in a respective slot 17 and 17'.
- Each cathode bar 3 or 3' is made of a conductive material, typically able to conduct the current from the cathode to the exterior Bus Bar.
- the material of these cathode bars is copper.
- the invention encompasses cathode bars made of other materials, such as for example steel, or other materials usually installed inside the cathode assemblies.
- the first step of said insertion process is the provision of a so called rough bar, which is shown on figure 5 and is referenced 5 as a whole.
- the dimensions of said rough bar 5 are globally analogous to those of final cathode bar 3, but slightly different.
- This bar 5, which has an elongated shape, is not shown with its real scale on figure 4 , in order to clearly illustrate the insertion process.
- the same remark applies to mechanical elements of figures 5 to 10 : slot 17, cathode bar 3 and bar elements 7 and 9, formed from rough bar 5.
- the width of these mechanical elements is far exaggerated with respect to their length.
- top views of figures 6 to 10 have been hatched to clearly distinguish the different mechanical elements.
- Rough bar 5 has front 51 and rear 52 walls, parallel upper and lower walls 53 and 54 , as well as parallel side walls 55 and 56. Respective length L5 , width W5 and height H5 of rough bar 5 are defined the same way as above length L1, width W1 and height H1 of cathode body 1 .
- Length L5 of rough bar is far superior to that L17 of slot 17 , so that final cathode bar 3 will protrude outside slot 17, above front wall 11.
- the value of the difference ( L5 - L17 ) implies the length of the protrusion of final cathode bar 3.
- this difference ( L5 - L17 ) is between 400 and 700 mm.
- Side walls 55 and 56 show slopes, the angle of which is similar to that aS of the side walls of the slot.
- the lengths of slotted parts of these side walls are referred L6 and L6' on figure 4 . Both L6 and L6' are superior to the length L17 of the cathode slot.
- the difference (L6 - L17) or (L6' - L17) is between 150 and 200 mm.
- width W5 of rough bar 5 is slightly superior to that W17 of slot 17 , which enables a steady jamming of final cathode bar 3 in the slot 17 .
- the difference ( W5 - W17 ) is between 5 to 10 mm.
- height H5 of rough bar 5 is equal or slightly inferior to depth D17 of cathode slot, so as to prevent final cathode bar from protruding outside the slot 17 , above lower wall 14.
- the difference ( D17 - H5 ) is between 0 and 4 mm.
- the insertion process then implies cutting rough bar 5, so as to form two cathode bar elements, or so called bar elements 7 and 9.
- Rough bar 5 is cut along a cutting line referenced CL, shown on figure 4 .
- This line CL forms an angle, noted ac, with the main longitudinal axis A5 of rough bar 5.
- this angle ac is between 1° and 4°, typically of about 2°.
- the cutting operation can be carried out by water jet cutting following a machining of the two surfaces, since the cut cannot be straight and the roughness will not be good enough to get a good contact between the two parts.
- Another way is cutting the two parts directly by machining using a circular cutting blade, typically of 3 to 6 mm of thickness. The latest way is preferred, since the cutting surface will present a good roughness and machining the cut surfaces will therefore not be necessary.
- first bar element 7 has a triangular shape. It has a front wall 71 , a main side wall 73 , as well as a tapered wall 77. It has neither a rear wall, nor a second side wall, since wall 77 directly connects both walls 71 and 73. Side wall 73 shows a slope, which corresponds to that of side wall 55 of rough bar 5.
- Width W7 is inferior to that W5 of rough bar 5, and is also slightly inferior to that W17 of the slot, so as to enable an insertion without jamming of said bar element 7 into slot 17 .
- the difference ( W17 - W7 ) is between 10 and 40 mm.
- Length L7 is far inferior to that L5 of rough bar 5, but is slightly superior to that L17 of slot, so as to enable a protrusion of said bar element 7 outside slot 17.
- the difference ( L7 - L17 ) is between 20 and 100 mm.
- height H7 of bar element 7 is equal to that H5 of rough bar 5.
- second bar element 9 has a shape which is different from a triangle. It has a short front wall 91 , a long rear wall 92 , a main side wall 93, a short side wall 94, as well as a tapered wall 97. Side wall 93 shows a slope, which corresponds to that of side wall 56 of rough bar 5.
- This second bar element can therefore be divided into two parts, namely a handling part 9A with constant width, as well as an insertion part or tip 9B , with a tapered shape.
- Tip 9B is ended by a shoulder 9C , formed adjacent front wall 91 , which eases the jamming of bars 7 and 9 into the slot.
- the respective dimensions of above defined walls and parts of bar element 9 are as follows:
- first bar element 7 is inserted into slot 17. It is to be noted that this step is carried out with a cathode block upside down. In other words, during said insertion, access to slot 17 is permitted from the end of the cathode block groove, whereas so called lower wall of cathode body is in an upper position.
- bar element 7 rests by gravity against wall 173 of this slot. Since W7 is inferior to W17 of slot, this insertion can be carried out easily, without jamming of said bar element 7 into slot 17.
- Bar element 7 is positioned in the slot, so that its front wall 71 is close to the end of the slot, and its main side wall 73 is adjacent side wall 172 of the slot. End of the slot is defined by the transition between rectilinear side walls 171 , 172 and rounded wall 174.
- main side wall 73 of first bar element 7 is urged against facing side wall 172 of slot 17 , along arrow F73
- main side wall 93 of second bar element 9 is urged against facing opposite side wall 171 of slot 17, along arrow F93.
- At least one and, preferably several welding lines are provided along the above defined contact line 37.
- four welding lines 21 to 24 are provided.
- L21 to L24 the length of each of these lines, as well as Lw the so called welding length, which corresponds to the sum ( L21 + L22 +L23 + L24 ) of the lengths of these lines.
- Each of L21 to L24 is typically between 50 and 100 mm, whereas the welding ratio, i.e ( Lw / L37 ) is between 10 and 40 %.
- Said global cathode bar has front 31 and rear 32 walls, as well as side walls 33 and 34.
- Said figure 8 also illustrates above described tapered line 37 , separating walls 77 and 97 of bar elements 7 and 9.
- First, rear wall 32 and side wall 34 are respectively constituted by those 92 and 94 of bar element 9.
- front wall 31 is formed by front wall 71 and front wall 91, as well as by a linking portion 77' of tapered wall 77.
- Front wall 91 is remote from end of slot, whereas front wall 71 is positioned against said end, as explained above.
- side wall 33 is formed by side wall 73 and side wall 93 , as well as by a linking portion 97' of tapered wall 97.
- Side wall 93 protrudes laterally, with respect to side wall 73 .
- Cathode can be decomposed into two portions, i.e. a first portion 3A the width of which W3A is equal to that W17 of slot 17 , as well as a second portion 3B the width of which W3B is equal to that W5 of rough bar 5 .
- This cathode defines a protrusion 3C , which extends outside slot 17 .
- This protrusion which is formed by portion 3B as well as by a fraction of portion 3A, has a typical length L3C between 400 and 700 mm.
- cathode bars 3 and 3' are positioned and jammed in their respective slot 17 and 17', the whole cathode assembly is turned upside down, so as to be in its final position of figure 1 . Due to the slopes of side walls of both the slots and the bar elements, as above described in reference to figure 11 , cathode bars cannot escape from their slots due to gravity, so that they are firmly retained therein.
- each side wall of cathode bar 3 directly contacts facing side walls of the slot 17 , i.e. without any intercalary material.
- the invention also encompasses alternative embodiments, wherein side walls of cathode bar indirectly contacts facing side walls of the slot. In this respect, a thin sheet of an intercalary material is interposed between said facing walls of slot and cathode bar.
- said intercalary material is a graphite foil, inserted between said facing side walls.
- This graphite foil is typically placed against the side walls of the slot, before insertion of bar elements.
- a further intercalary material, in particular at least one further graphite foil, may also be interposed between upper wall 173 of said slot and facing walls of the bar elements 7 and 9.
- one single intercalary graphite foil may recover both side walls and upper wall of the slot. The adjustment will be set, so that no substantial gap or space is left between bar elements, graphite foil and cathode body.
- Said graphite foil can be a flexible graphite foil of compressed expanded graphite.
- Said foil is available from various suppliers under different trademarks, such as PAPYEX® by MERSEN.
- the density of the foil is typically 0.7 and it may have 0.5 mm of thickness.
- graphite material is compressible to cope with the thermal expansion of bar elements.
- the selected electrolysis cell was provided with new cathode blocks; seventeen cathode assemblies were used, and the assembly n° 2,7,11, and 16 had copper cathode bars according to the invention, whereas the other ones were provided with conventional steel cathode bars.
- Cathode assemblies n° 2 and 7 had a sheet of graphite foil between the cathode bar and the cathode block, whereas assemblies n° 11 and 16 had a direct contact between the copper cathode bar and the cathode material. All cathode bars were half bars. Contact tabs were made from copper.
- the cell was started up according to conventional practice and run for about 3.5 months under production conditions (211 kA). Its overall performance was slightly better than that of the other cells with 100 % conventional cathode assemblies: as an example, compared to conventional D18 cells of the same potline, the average net voltage was slightly lower (60 mV), the aluminium purity was identical (99.873 %), aluminium production was slightly higher, specific energy consumption was lower (approximately 300 kW/h per ton), bath height and metal height as well as bath temperature (958 °C) were comparable, cell stability was comparable, base resistance set point and cathode voltage drop were slightly lower (approximately 20 mV).
- cathode assemblies with copper bars according to the invention were pulling about 40 % more current than cathode assemblies with steel bars in the same cell. This demonstrates that a significant gain can be obtained by constructing a pot equipped with all cathodes having full copper bars. At the beginning of the operations, a small difference was observed between copper cathode bars in direct contact with the cathode block and copper cathodes bars with an intercalary graphite foil, giving the benefit to the latest.
- the cell was then autopsied; the copper bars could be easily cut out, and it was found that for each half bar the two bar elements were firmly welded together at their tapered interface and did not separate upon removal. This shows that the electrical contact at the tapered interface between the two bar elements was excellent. No melting of the copper bar was observed, no significant visual change was observed. Slight remains of graphite foil were visible on the collector bar side for the two bars that had been in contact with graphite foil. The copper could be fully recovered for recycling.
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)
Description
- The invention relates to the field of fused salt electrolysis using the Hall-Heroult process for making aluminium. More specifically it relates to the improvement of the cathode blocks of such an electrolysis cell, the improvement being related to the cathode drop and the current distribution along the cathode blocks. In particular, the invention relates to an improvement for cathode block provided with a cathode collector bar.
- The Hall-Héroult process is the only continuous industrial process for producing metallic aluminium from aluminium oxide. Aluminium oxide (Al2O3) is dissolved in molten cryolite (Na3AlF6), and the resulting mixture (typically at a temperature comprised between 940 °C and 970 °C) acts as a liquid electrolyte in an electrolytic cell. An electrolytic cell (also called "pot") used for the Hall-Heroult process typically comprises a steel shell (so-called pot shell), a lining (comprising refractory bricks protecting said steel shell against heat, and cathode blocks usually made from graphite, anthracite or a mixture of both), and a plurality of anodes (usually made from carbon) that plunge into the liquid electrolyte contained in the volume defined by the cathode bottom and a side lining made from carbonaceous material. Anodes and cathodes are connected to external busbars. An electrical current is passed through the cell (typically at a voltage between 3.5 V and 5 V) which electrochemically reduces the aluminium oxide, split in the electrolyte into aluminium and oxygen ions, then into aluminium at the cathode and oxygen at the anode; said oxygen reacting with the carbon of the anode to form carbon dioxide. The resulting metallic aluminium is not miscible with the liquid electrolyte, has a higher density than the liquid electrolyte and will thus accumulate as a liquid metal pad on the cathode surface below the electrolyte from where it needs to be removed from time to time, usually by suction into a crucible.
- Industrial electrolytic cells used for the Hall-Heroult process are generally rectangular in shape and connected electrically in series, the ends of the series being connected to the positive and negative poles of an electrical rectification and control substation. The general outline of these cells is known to a person skilled in the art and will not be repeated here in detail. They have a length usually comprised between 8 and 25 meters and a width usually comprised between 3 and 5 meters. The cells (also called "pots") are always operated in series of several tens (up to several hundreds) of pots (such a series being also called a "potline"); within each series DC currents flow from one cell to the neighbouring cell. The electrical currents in most modern electrolytic cells using the Hall-Héroult process exceed 200 kA and can reach 400 kA, 450 kA or even more; in these potlines the pots are arranged side by side. Most newly installed pots operate at a current comprised between about 350 kA and 600 kA, and more often in the order of 400 kA to 500 kA. The passage of these enormous current intensities through the electrolytic cell leads to ohmic losses at various locations of the pot and its environment.
- Cathode assemblies for use in electrolytic cells suitable for the Hall-Heroult process are industrially manufactured for more than a century, and the state of the art is summarized in the reference book " Cathodes in Aluminium Electrolysis" by M. Sørlie and H. Øye, 3rd edition (Düsseldorf 2010). They comprise a cathode body made from a carbon material and one or more metallic cathode bars that are fitted into slots or grooves machined into the lower surface of said carbon body. Said metallic cathode bar protrudes out of each end of the cathode block, thereby allowing to connect the cathode assembly to the cathode busbar system. The metallic cathode bar is usually mode from steel; copper inserts within the steel bar can be used in order to increase the electrical conductivity of the cathode bar. Said steel bars are inserted into grooves that are wider than the steel bars, and then fixed with electrically conductive glue (carbonaceous glue or cement, or ramming paste) or with cast iron that is poured into the interstitial space between the steel bar and the carbon body, as described in
GB 663 763 - Other prior art designs of cathode assemblies are described in
US 6 294 067 ,EP 1 845 174US 4 795 540 ,US 2004 0011661 ,CN 105 671 592 ,SU 1 260 412GB 1 065 080CN 2 892 888 , andUS 5 976 333 . - During the past decades, much effort has been devoted to the decrease of ohmic losses in cathode bars. Most inventions reported in prior art patents focus on the intrinsic conductivity of the steel cathode bar, or on the contact resistance between the cathode bar and the cathode block or between the cathode bar and the aluminium busbar.
- A cathode with a full copper cathode bar inlaid into a groove machined in the lower surface of the carbon body is known from
WO 2016/079605 (Kan Nak s.a.), in particularfigures 7 and9 of said document. The contact between the carbon body and the copper bar is critical for the electrical performance of the electrolysis cell. Copper has a much higher thermal expansion coefficient than the carbon material of the cathode block body, and the copper bar in direct contact with the carbon body will operate at a temperature that is probably less than 100°C lower than its melting point, leading to significant thermal expansion. As a consequence, a well-defined allowance for thermal expansion must be groove is required in order to ensure a good and reliable electrical contact between the copper bar and the carbon body over the whole length. Reliability of this contact is of paramount importance, because once installed into a cell and the cell started, a cathode block cannot be repaired, and cannot be replaced without relining of the whole cell. The normal lifetime of a cathode lining is comprised between five and seven years. - Usually, large carbon products such as cathodes for use in Hall-Heroult cells are machined with a tolerance of ± 2 mm; a tolerance of ± 1 mm can be reached, but at a high cost. The applicant has found that it is very difficult to get reliable contacts by inserting metallic bar, in particular copper bar, directly into grooves machined into the carbon bodies without using glue.
- The problem addressed by the present invention is therefore to improve the quality and reliability of the electrical contact of metallic bars, in particular copper bars, inserted into grooves machined into the carbon body of a cathode block.
- A first object of the invention is a cathode assembly suitable for a Hall-Heroult electrolysis cell, comprising
- a cathode body made of a carbonaceous material, said cathode body being provided with at least one slot, said slot being provided with side walls parallel to a longitudinal direction of said slot;
- at least one cathode collector bar made of a metallic material, said cathode bar being provided with side walls, which are in contact with said side walls of said slot;
- Advantageously, said cathode assembly is provided with fixation means, in particular permanent fixation means, between said tapered walls of said bar elements. Said fixation means are advantageously welding means. In one embodiment, said welding means comprise at least one welding line, in particular several welding lines, extending over at least part of said contact line.
- In an advantageous embodiment, said cathode body is provided with at least one first and one second slots, each slot being provided with a blind wall defining a longitudinal end of said slot, each slot receiving a respective cathode bar. Advantageously, said cathode bar is jammed against said longitudinal end of a respective slot.
- In one embodiment, one first bar element has a triangular shape and comprises a front wall, said main side wall and said tapered wall. Advantageously, one second bar element comprises a further side wall, opposite to main side wall, said further side wall protruding with respect to main side wall of first bar element, along a transversal direction of said slot.
- In an advantageous embodiment said front wall of first bar element is positioned against longitudinal end of said slot, and said second bar element comprises a front wall, the length of which is far inferior to that of front wall of first bar element, front wall of second bar element being remote from end of said slot.
- In one embodiment said cathode bar has two portions, i.e. a first portion the width of which is equal to that of slot, as well as a second portion the width of which is superior to that of slot.
- In an advantageous embodiment said cathode bar has a protrusion which extends outside said slot. Said protrusion is in particular formed by said second portion and by a fraction of said first portion. In one embodiment main side wall of each bar element protrudes outside said slot.
- In one embodiment main side wall of each bar element directly contacts a respective side wall of said slot.
- In an alternative embodiment main side wall of each bar element indirectly contacts a respective side wall of said slot, an intercalary material, in particular at least one graphite foil, being interposed between said main side wall and said respective side wall of said slot. A further intercalary material, in particular at least one further graphite foil, may be interposed between upper wall of said slot and facing walls of bar elements.
- In an advantageous embodiment said side walls of said slot and said side walls of said bar elements show a slope, the value of which is in particular of about 10 degrees, so as to retain said bar elements in the inner volume of said slot.
- Said cathode bar is advantageously made of copper. In an alternative embodiment said cathode bar is made of steel.
- Another object of the present invention is a process for making a cathode assembly as described above, comprising the steps of
- a) providing a cathode body made of a carbonaceous material;
- b) providing at least one slot in said cathode body, said slot being provided with side walls parallel to a longitudinal direction of said slot;
- c) providing at least two bar elements made of a metallic material, each bar element being provided with a main side wall and a tapered wall,
- d) placing a first bar element into the slot, with its main side wall adjacent to facing first side wall of the slot;
- e) urging forward, substantially along said longitudinal direction of said slot, second bar element, so as to urge main side wall of said first bar element against facing first side wall of the slot, so as to urge main side wall of said second bar element against facing opposite second side wall of the slot, and so as to set into contact the two tapered walls of said bar elements, along a contact line.
- In an advantageous embodiment urging forward said second bar element also provokes the jamming of said first bar element against one longitudinal end of said slot.
- In an advantageous embodiment said process further comprises providing said side walls of said slot and said side walls of said bar elements with a slope, the value of which is in particular of about 10 degrees, so as to retain said bar elements in the inner volume of said slot.
- In an advantageous embodiment second bar element is provided with a handling portion and said second bar is urged forward manually, by handling said handling portion.
- In an advantageous embodiment bar elements are provided by cutting a rough bar along a cutting line, said cutting line being tapered with respect to main axis of said rough bar.
- In an advantageous embodiment said process further comprises providing fixation means, in particular permanent fixation means, between said tapered walls of said bar elements, once said tapered walls of said bar elements are in mutual contact.
- Another object of the present invention is an electrolytic cell suitable for the Hall-Heroult electrolysis process, comprising
a cathode forming the bottom of said electrolytic cell and comprising a plurality of parallel cathode assembly, each cathode assembly comprising at least one metallic cathode collector bar protruding out of each of the two ends of the cathode,
a lateral lining defining together with the cathode a volume containing the liquid electrolyte and the liquid metal resulting from the Hall-Heroult electrolysis process,
an outer metallic potshell containing said cathode and lateral lining,
a plurality of anode assemblies suspended above the cathode, each anode assembly comprising at least one anode and at least one metallic anode rod connected to an anode beam,
a cathodic bus bar surrounding said potshell, said bus bar being connected to at least part of said cathode assemblies
said electrolytic cell being characterized in that
at least one of said cathode assembly, and preferably more than 60% of said cathode assemblies and, more preferably, each of said cathode assemblies, is a cathode assembly as described above. - Another object of the present invention is an electrolytic cell for the production of aluminium by the Hall-Heroult process, comprising at least one cathode assembly as described above.
- Another object of the present invention is a process for making aluminium by the Hall-Héroult process, using an electrolytic cell provided with cathode assemblies as described above.
-
-
Figures 1 to 11 represent one embodiment of the present invention. -
Figure 1 is a perspective view, showing one embodiment of a cathode assembly according to the invention. -
Figure 2 is a perspective view, showing upside down a cathode body which belongs to said cathode assembly according to the invention, saidfigure 2 showing in particular slots provided in said cathode body. -
Figure 3 is a longitudinal section showing the cathode body offigure 2 . -
Figure 4 is a top view, showing at a greater scale a rough bar from which a cathode bar is formed, said cathode assembly offigure 1 being equipped with said cathode bar. -
Figure 5 is a top view, analogous tofigure 4 , showing a cutting operation of said rough bar offigure 4 , in order to form two bar elements. -
Figures 6 and 7 are top views, analogous tofigure 5 , showing two steps of the insertion of said bar elements into a slot of said cathode body. -
Figure 8 is a top view, analogous tofigures 6 and 7 , showing the final cathode bar of the cathode assembly according to the invention, said cathode bar being formed from said bar elements once inserted in said slot and mutually attached. -
Figures 9 and 10 are top views, showing at still a greater scale the details IX and X offigure 8 . -
Figure 11 is a cross section showing the cathode bar offigure 8 , along line XI-XI offigure 8 . - The following reference signs are used on the figures:
C Cathode assembly 1 Cathode body 11,12 Front/rear wall of cathode body 1 171, 172 Side walls of slot 17 13,14 Upper/lower wall of cathode body 1 173 Top wall of slot 17,17' 15,16 Side walls of cathode body 1 174,174' Blind wall of slot 17,17' 17, 17' Slots in cathode body 1 D174 Distance between 174 174' 3,3' Cathode bar 31,32 Front/rear wall of cathode bar 3 33,34 Side walls of cathode bar 3 37 Contact line of 3 5 Rough bar 51,52 Front / rear wall of rough bar 5 53,54 Upper / lower wall of rough bar 5 55,56 Side walls of rough bar 5 A5 Axis of rough bar 5 CL Cutting line L6 Length of slotted bar αs Angle of slotted bar αc Angle between A5 and CL A17,A17' Axis of slots 17, 17' 7, 9 Bar elements 9A Handling part of 9 9B Tip of 9 9C Shoulder of 9 71 Front wall of bar element 7 91,92 Front / rear wall of bar element 9 73 Side wall of bar element 7 93,94 Side walls of bar element 9 77 Tapered wall of bar element 7 97 Tapered wall of bar element 9 F9, S9 Motion of 9 F73, F93 Motion of 73,93 21-24 Welding lines 3A,3B Portions of 3 3C Protrusion of 3 77',97' Linking portion of 77,97 D17,D1 7' Depth of 17, 17' H1 Height of 1 LX Length of element X : L1, L17, L17', L5, L7, L93, L94, L37, L3C' WX Width of element X : W1, W5, W17, W17', W7, W91, W92 - In the present description, the terms "upper" and "lower" refer to a cathode block in the position of its industrial use, lying on a horizontal ground surface, i.e. the upper surface being intended to be in contact with the liquid aluminium in the electrolysis cell. Moreover, unless specified otherwise, "conductive" means "electrically conductive". According to the terminology used in the art, a "cathode assembly" C comprises a
cathode body 1 and at least onecathode bar 3. - The present invention is first applicable to cathode assemblies C comprising a
cathode body 1 and at least onecathode bar 3 and 3'. In particular, the invention is applicable to cathode assemblies comprising twocathode bars 3,3', one 3 of which is protruding out of thefront wall 11, the other 3' protruding out of therear wall 12 of thecathode body 1. These cathode bars, which are half bars, form two portions of a so-called "split bar" in the sense that they are not through bars, i.e. each cathode bar is not extending through the whole length of the cathode block. - The present invention is also applicable to cathode assemblies having one (or more) through bar(s) instead of above defined split bars. The invention applies in particular to such through bars, which have a short length. However, the use of split bars is preferred, since it allows a better jamming of these bars, as will appear at reading the following description.
- The present invention applies to cathodes used in the Hall-Heroult process that form the bottom of an electrolysis cell, said cathodes being assembled from individual cathode assemblies C, each of which bears at least one
cathode bar 3, 3'. The Hall-Heroult process and the outline of an electrolysis cell (also called "pot") are known to a person skilled in the art and will not be described here in great detail. The invention will be explained in relation with embodiments comprising one split cathode bar per cathode assembly C, said split cathode bar comprising twoportions 3, 3' but it is understood that the present invention can be applied to cathode assemblies C comprising any number of split cathode bars withportions 3, 3', such as two sets of split bars arranged parallel to each other. In the following the portion of a split cathode bar will be referred to as the "cathode bar". - The cathode assembly of the invention is designated as a whole by alphanumeric reference C. It is suitable for a Hall-Heroult electrolysis cell, but could be used in other electrolytic processes.
- The cathode assembly C first comprises a
cathode body 1, of known type, which is made of a carbonaceous material, typically graphitized carbon or graphite. Thiscathode body 1, which has an elongated shape, has opposite end walls, i.e.front 11 and rear 12 walls, as well as peripheral walls. The latter are formed by parallel upper andlower walls parallel side walls figure 3 ), i.e. the distance betweenwalls figure 2 ), i.e. the distance betweenwalls figure 3 ), i.e. the distance betweenwalls - As more clearly shown on
figures 2 and 3 , thelower wall 14 ofcathode body 1 is provided with two housings, each being formed by a respectivelongitudinal slot 17 and 17', the longitudinal main axis of which is referenced A17, A17'.Figure 2 shows cathode body "upside down", with reference to its above defined industrial use position. - Each
slot 17, 17' is provided withopposite side walls figure 2 ), parallel to said main axis A17, A17', whereas its top wall is referenced 173, 173' (seefigure 3 ). Moreover eachslot 17, 17' is provided with a respective rear wall, orblind wall 174, 174' (seefigure 2 ), each defining a respective longitudinal end of said slot. The distance D174 (seefigure 3 ) between these two walls is typically between 200 millimetres (mm) and 600 mm. Viewed from bottom,blind wall 174, 174' is rounded, which makes it possible to ease the slot machining.First slot 17 does lead tofront wall 11 of this cathode body, whereas second slot 17' does lead torear wall 12 of this cathode body. - By way of example, width W17 or W17' (see
figure 2 ) of eachslot 17, 17', i.e. the distance between side walls, is between about 50 mm and about 250 mm. Advantageously, as illustrated in particular onfigure 11 , eachside wall top wall 173, 173' of this slot tolower wall 14 of cathode body. As will be described hereafter, these slopes make it possible to maintain the bar elements in the inner volume of the slot, when turning over the cathode assemblies. For sake of clarity, the value of as is exaggerated on thisfigure 11 . - By way of example, depth D17 or D17' of each
slot 17, 17' (seefigure 3 ), i.e. the distance betweentop wall 173, 173' and the surface oflower wall 14 of thebody 1, is between about 50 mm and about 150 mm. By way of example, its length L17 or L17' (seefigure 3 ), i.e. the distance between front wall or rear wall of cathode body andblind wall 174, 174', is between about 1200 mm and about 1850 mm. This length is taken from the junction of rounded portion of said blind wall with rectilinear part ofside walls - The cathode assembly C also comprises two
cathode bars 3 and 3' (schematically shown onfigure 1 ), each of which is accommodated in arespective slot 17 and 17'. Eachcathode bar 3 or 3' is made of a conductive material, typically able to conduct the current from the cathode to the exterior Bus Bar. Advantageously, the material of these cathode bars is copper. However, the invention encompasses cathode bars made of other materials, such as for example steel, or other materials usually installed inside the cathode assemblies. The insertion process ofcathode bar 3 into itsslot 17 will now be described, bearing in mind that insertion process of other cathode bar 3' into other slot 17' is identical. - The first step of said insertion process is the provision of a so called rough bar, which is shown on
figure 5 and is referenced 5 as a whole. As will appear more clearly at reading the next steps of this process, the dimensions of saidrough bar 5 are globally analogous to those offinal cathode bar 3, but slightly different. Thisbar 5, which has an elongated shape, is not shown with its real scale onfigure 4 , in order to clearly illustrate the insertion process. The same remark applies to mechanical elements offigures 5 to 10 :slot 17,cathode bar 3 andbar elements rough bar 5. In particular, the width of these mechanical elements is far exaggerated with respect to their length. Moreover, top views offigures 6 to 10 have been hatched to clearly distinguish the different mechanical elements. -
Rough bar 5 hasfront 51 and rear 52 walls, parallel upper andlower walls parallel side walls rough bar 5 are defined the same way as above length L1, width W1 and height H1 ofcathode body 1. - Length L5 of rough bar is far superior to that L17 of
slot 17, so thatfinal cathode bar 3 will protrude outsideslot 17, abovefront wall 11. The value of the difference (L5 - L17) implies the length of the protrusion offinal cathode bar 3. Typically, this difference (L5 - L17) is between 400 and 700 mm.Side walls figure 4 . Both L6 and L6' are superior to the length L17 of the cathode slot. Typically, the difference (L6 - L17) or (L6' - L17) is between 150 and 200 mm. - In addition, width W5 of
rough bar 5 is slightly superior to that W17 ofslot 17, which enables a steady jamming offinal cathode bar 3 in theslot 17. Typically, the difference (W5 - W17) is between 5 to 10 mm. - Finally, height H5 of
rough bar 5 is equal or slightly inferior to depth D17 of cathode slot, so as to prevent final cathode bar from protruding outside theslot 17, abovelower wall 14. Typically, the difference (D17 - H5) is between 0 and 4 mm. - The insertion process then implies cutting
rough bar 5, so as to form two cathode bar elements, or so calledbar elements Rough bar 5 is cut along a cutting line referenced CL, shown onfigure 4 . This line CL forms an angle, noted ac, with the main longitudinal axis A5 ofrough bar 5. By way of example, this angle ac is between 1° and 4°, typically of about 2°. The cutting operation can be carried out by water jet cutting following a machining of the two surfaces, since the cut cannot be straight and the roughness will not be good enough to get a good contact between the two parts. Another way is cutting the two parts directly by machining using a circular cutting blade, typically of 3 to 6 mm of thickness. The latest way is preferred, since the cutting surface will present a good roughness and machining the cut surfaces will therefore not be necessary. - As shown on
figure 5 ,first bar element 7 has a triangular shape. It has afront wall 71, amain side wall 73, as well as atapered wall 77. It has neither a rear wall, nor a second side wall, sincewall 77 directly connects bothwalls Side wall 73 shows a slope, which corresponds to that ofside wall 55 ofrough bar 5. - Let us note length L7 and width W7 of said
bar element 7. Width W7 is inferior to that W5 ofrough bar 5, and is also slightly inferior to that W17 of the slot, so as to enable an insertion without jamming of saidbar element 7 intoslot 17. Typically, the difference (W17 - W7) is between 10 and 40 mm. Length L7 is far inferior to that L5 ofrough bar 5, but is slightly superior to that L17 of slot, so as to enable a protrusion of saidbar element 7 outsideslot 17. Typically, the difference (L7 - L17) is between 20 and 100 mm. Finally, height H7 ofbar element 7 is equal to that H5 ofrough bar 5. - As also shown on
figure 5 ,second bar element 9 has a shape which is different from a triangle. It has a shortfront wall 91, a longrear wall 92, amain side wall 93, ashort side wall 94, as well as atapered wall 97.Side wall 93 shows a slope, which corresponds to that ofside wall 56 ofrough bar 5. - This second bar element can therefore be divided into two parts, namely a
handling part 9A with constant width, as well as an insertion part ortip 9B, with a tapered shape.Tip 9B is ended by ashoulder 9C, formed adjacentfront wall 91, which eases the jamming ofbars bar element 9 are as follows: - W92 (width of 92) = W5;
- L93 (length of 93) = L5;
- L94 (length of 94) = L5 - L7;
- H9 (height of 9) = H5.
- According to next step of the process of the invention, shown on
figure 6 ,first bar element 7 is inserted intoslot 17. It is to be noted that this step is carried out with a cathode block upside down. In other words, during said insertion, access to slot 17 is permitted from the end of the cathode block groove, whereas so called lower wall of cathode body is in an upper position. Once inserted in the slot,bar element 7 rests by gravity againstwall 173 of this slot. Since W7 is inferior to W17 of slot, this insertion can be carried out easily, without jamming of saidbar element 7 intoslot 17.Bar element 7 is positioned in the slot, so that itsfront wall 71 is close to the end of the slot, and itsmain side wall 73 isadjacent side wall 172 of the slot. End of the slot is defined by the transition betweenrectilinear side walls rounded wall 174. - Then an operator handles
second bar element 9, at thehandling part 9A thereof. The operator pushesbar element 9 forward, i.e. towards the end of the slot, along arrow F9. At an intermediate stage of this forward pushing motion, the facing taperedwalls figure 7 ). Sincefirst bar element 7 is axially jammed by the end of the slot,second bar element 9 slides with respect to barelement 7 along arrow S9, so that the global motion ofbar element 9 now comprises a tapered component. Due to this sliding motion, bothbar elements slot 17. More precisely,main side wall 73 offirst bar element 7 is urged against facingside wall 172 ofslot 17, along arrow F73, whereasmain side wall 93 ofsecond bar element 9 is urged against facingopposite side wall 171 ofslot 17, along arrow F93. In the above paragraph, insertion operation has been described manually. However, an automatic operation may be considered, with any appropriate tool. - Once
bar elements slot 17, their taperedwalls figure 8 ). The length L37 of contact line is slightly inferior to both L77 and L97, since one short end region of eachwall other wall bar element 9 with respect to thefirst bar element 7 already installed. When the protrusion of the bars outside the cathode L3C is adjusted at the required value, then the twobar elements - Referring to
figure 8 , at least one and, preferably several welding lines are provided along the above definedcontact line 37. In the illustrated example, fourwelding lines 21 to 24 are provided. Let us note L21 to L24 the length of each of these lines, as well as Lw the so called welding length, which corresponds to the sum (L21 + L22 +L23 + L24) of the lengths of these lines. Each of L21 to L24 is typically between 50 and 100 mm, whereas the welding ratio, i.e (Lw / L37) is between 10 and 40 %. - After above described welding step,
bar elements final cathode bar 3 shown onfigure 8 . Said global cathode bar hasfront 31 and rear 32 walls, as well asside walls figure 8 also illustrates above described taperedline 37, separatingwalls bar elements rear wall 32 andside wall 34 are respectively constituted by those 92 and 94 ofbar element 9. - Moreover, as shown by
detail 9,front wall 31 is formed byfront wall 71 andfront wall 91, as well as by a linking portion 77' of taperedwall 77.Front wall 91 is remote from end of slot, whereasfront wall 71 is positioned against said end, as explained above. In addition, as shown by detail 10,side wall 33 is formed byside wall 73 andside wall 93, as well as by a linking portion 97' of taperedwall 97.Side wall 93 protrudes laterally, with respect toside wall 73. - Cathode can be decomposed into two portions, i.e. a
first portion 3A the width of which W3A is equal to that W17 ofslot 17, as well as asecond portion 3B the width of which W3B is equal to that W5 ofrough bar 5. This cathode defines aprotrusion 3C, which extends outsideslot 17. This protrusion, which is formed byportion 3B as well as by a fraction ofportion 3A, has a typical length L3C between 400 and 700 mm. - Once
cathode bars 3 and 3' are positioned and jammed in theirrespective slot 17 and 17', the whole cathode assembly is turned upside down, so as to be in its final position offigure 1 . Due to the slopes of side walls of both the slots and the bar elements, as above described in reference tofigure 11 , cathode bars cannot escape from their slots due to gravity, so that they are firmly retained therein. - In the above described embodiment, each side wall of
cathode bar 3 directly contacts facing side walls of theslot 17, i.e. without any intercalary material. The invention also encompasses alternative embodiments, wherein side walls of cathode bar indirectly contacts facing side walls of the slot. In this respect, a thin sheet of an intercalary material is interposed between said facing walls of slot and cathode bar. - According to an advantageous embodiment of the invention, said intercalary material is a graphite foil, inserted between said facing side walls. This graphite foil is typically placed against the side walls of the slot, before insertion of bar elements. A further intercalary material, in particular at least one further graphite foil, may also be interposed between
upper wall 173 of said slot and facing walls of thebar elements - An industrial trial was carried out using an electrolysis cell of the so-called D18 technology; this cell was part of an existing D18 potline. The D18 technology has been described in several papers such as: " Update on the development of D18 cell technology at DUBAL" (D. Whitfiled et al., Light Metals 2012, p. 727-731); " D18+: potline modernization at DUBAL" (S. Akhmetov et al., Light Metals 2013, p. 561-656); " From D18 to D18+: Progression of DUBAL's original potlines" (D. Whitfield et al., Light Metals 2015, p. 499-504). The selected electrolysis cell was provided with new cathode blocks; seventeen cathode assemblies were used, and the assembly n° 2,7,11, and 16 had copper cathode bars according to the invention, whereas the other ones were provided with conventional steel cathode bars. Cathode assemblies n° 2 and 7 had a sheet of graphite foil between the cathode bar and the cathode block, whereas assemblies n° 11 and 16 had a direct contact between the copper cathode bar and the cathode material. All cathode bars were half bars. Contact tabs were made from copper.
- The cell was started up according to conventional practice and run for about 3.5 months under production conditions (211 kA). Its overall performance was slightly better than that of the other cells with 100 % conventional cathode assemblies: as an example, compared to conventional D18 cells of the same potline, the average net voltage was slightly lower (60 mV), the aluminium purity was identical (99.873 %), aluminium production was slightly higher, specific energy consumption was lower (approximately 300 kW/h per ton), bath height and metal height as well as bath temperature (958 °C) were comparable, cell stability was comparable, base resistance set point and cathode voltage drop were slightly lower (approximately 20 mV).
- It was found that the cathode assemblies with copper bars according to the invention were pulling about 40 % more current than cathode assemblies with steel bars in the same cell. This demonstrates that a significant gain can be obtained by constructing a pot equipped with all cathodes having full copper bars. At the beginning of the operations, a small difference was observed between copper cathode bars in direct contact with the cathode block and copper cathodes bars with an intercalary graphite foil, giving the benefit to the latest.
- The cell was then autopsied; the copper bars could be easily cut out, and it was found that for each half bar the two bar elements were firmly welded together at their tapered interface and did not separate upon removal. This shows that the electrical contact at the tapered interface between the two bar elements was excellent. No melting of the copper bar was observed, no significant visual change was observed. Slight remains of graphite foil were visible on the collector bar side for the two bars that had been in contact with graphite foil. The copper could be fully recovered for recycling.
Claims (15)
- A cathode assembly (C) suitable for a Hall-Heroult electrolysis cell, comprising- a cathode body (1) made of a carbonaceous material, said cathode body being provided with at least one slot (17, 17'), said slot being provided with side walls (171, 172, 171', 172') parallel to a longitudinal direction (A17, A17') of said slot;- at least one cathode collector bar (3, 3') made of a metallic material, said cathode bar being provided with side walls (33, 34), which are in contact with said side walls of said slot;characterized in that said cathode bar comprises two bar elements (7, 9), each bar element being provided with a main side wall (73, 93) which is in contact with a respective side wall (171, 172) of said slot, as well as a tapered wall (77, 97), the two tapered walls of said bar elements forming a contact line (37) between these two bar elements.
- A cathode assembly according to claim 1, characterized in that it is provided with fixation means, in particular permanent fixation means (21-24) such as welding means, between said tapered walls (77, 97) of said bar elements (7, 9).
- A cathode assembly according to claim 2, characterized in that said welding means comprise at least one welding line, in particular several welding lines (21-24), extending over at least part of said contact line (37).
- A cathode assembly according to any above claim, characterized in that one first bar element (7) has a triangular shape and comprises a front wall (71), said main side wall (73) and said tapered wall (77).
- A cathode assembly according to any above claim, characterized in that one second bar element (9) comprises a further side wall (94), opposite to main side wall (93), said further side wall protruding with respect to main side wall (73) of first bar element (7), along a transversal direction of said slot.
- A cathode assembly according to any above claim, characterized in that said cathode bar (3) has two portions, i.e. a first portion (3A) the width of which (W3A) is equal to that of slot (17), as well as a second portion (3B) the width of which (W3B) is superior to that of slot.
- A cathode assembly according to claim 6, characterized in that said cathode bar has a protrusion (3C) which extends outside said slot (17).
- A cathode assembly according to claim 7, characterized in that said protrusion (3C) is formed by said second portion (3C) and by a fraction of said first portion (3A).
- A cathode assembly according to any of claims 1 to 8, characterized in that said main side wall of each bar element indirectly contacts a respective side wall of said slot, an intercalary material, in particular at least one graphite foil, being interposed between said main side wall and said respective side wall of said slot, and optionally a further intercalary material, in particular at least one further graphite foil, is interposed between upper wall (173) of said slot and facing walls of bar elements (7, 9).
- A cathode assembly according to any above claim, characterized in that said side walls (171, 171', 172, 172') of said slot and said side walls (73, 93) of said bar elements (7, 9) show a slope, the value (αs) of which is in particular of 10 degrees, so as to retain said bar elements in the inner volume of said slot.
- A process for making a cathode assembly (C) according to any of above claims, comprising the steps ofa) providing a cathode body (1) made of a carbonaceous material;b) providing at least one slot (17, 17') in said cathode body, said slot being provided with side walls (171, 171', 172, 172') parallel to a longitudinal direction of said slot;c) providing at least two bar elements (7, 9) made of a metallic material, each bar element being provided with a main side wall (73, 93) and a tapered wall (77, 97),d) placing a first bar element (7) into the slot, with its main side wall (73) adjacent to facing first side wall (172) of the slot;e) urging forward, along said longitudinal direction of said slot, second bar element (9), so as to urge main side wall (73) of said first bar element against facing first side wall (172) of the slot, so as to urge main side wall (93) of said second bar element (9) against facing opposite second side wall (171) of the slot, and so as to set into contact the two tapered walls (77, 97) of said bar elements, along a contact line (37).
- A process according to claim 11, further comprising providing said side walls (171, 171', 172, 172') of said slot and said side walls (73, 93) of said bar elements (7, 9) with a slope, the value (αs) of which is in particular of 10 degrees, so as to retain said bar elements in the inner volume of said slot.
- A process according to any of claims 11 to 12, wherein said second bar element (9) is provided with a handling portion (9A), and wherein said second bar element is urged forward manually, by handling said handling portion.
- A process according to any of claims 11 to 13, wherein said bar elements are provided by cutting a rough bar (5) along a cutting line (CL), said cutting line being tapered with respect to main axis (A5) of said rough bar.
- A process for making aluminium by the Hall-Heroult process, using an electrolytic cell provided with cathode assemblies according to any of claims 1 to 10.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL18741304T PL3571333T3 (en) | 2017-01-23 | 2018-01-18 | Cathode assembly with metallic collector bar for electrolytic cell suitable for the hall-héroult process |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1701067.9A GB2558936A (en) | 2017-01-23 | 2017-01-23 | Cathode assembly with metallic collector bar for electrolytic cell suitable for the Hall-Héroult process |
PCT/IB2018/050300 WO2018134754A1 (en) | 2017-01-23 | 2018-01-18 | Cathode assembly with metallic collector bar for electrolytic cell suitable for the Hall-Héroult process |
Publications (3)
Publication Number | Publication Date |
---|---|
EP3571333A1 EP3571333A1 (en) | 2019-11-27 |
EP3571333A4 EP3571333A4 (en) | 2020-09-09 |
EP3571333B1 true EP3571333B1 (en) | 2021-08-18 |
Family
ID=58462950
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP18741304.2A Active EP3571333B1 (en) | 2017-01-23 | 2018-01-18 | Cathode assembly with metallic collector bar for electrolytic cell suitable for the hall-héroult process |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP3571333B1 (en) |
CA (1) | CA3049822C (en) |
GB (1) | GB2558936A (en) |
PL (1) | PL3571333T3 (en) |
WO (1) | WO2018134754A1 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2595460A (en) * | 2020-05-26 | 2021-12-01 | Dubai Aluminium Pjsc | Cathode assembly with metallic collector bar systems for electrolytic cell suitable for the Hall-Héroult process |
WO2023119802A1 (en) | 2021-12-23 | 2023-06-29 | Secカーボン株式会社 | Cathode assembly |
JP2024024213A (en) * | 2022-08-09 | 2024-02-22 | Secカーボン株式会社 | cathode assembly |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1065080A (en) * | 1964-06-30 | 1967-04-12 | Reynolds Metals Co | Improvements in or relating to aluminium reduction pots |
US4795540A (en) * | 1987-05-19 | 1989-01-03 | Comalco Aluminum, Ltd. | Slotted cathode collector bar for electrolyte reduction cell |
US5976333A (en) * | 1998-01-06 | 1999-11-02 | Pate; Ray H. | Collector bar |
US6294067B1 (en) * | 2000-03-30 | 2001-09-25 | Alcoa Inc. | 3 component cathode collector bar |
US6866768B2 (en) * | 2002-07-16 | 2005-03-15 | Donald R Bradford | Electrolytic cell for production of aluminum from alumina |
DE10261745B3 (en) * | 2002-12-30 | 2004-07-22 | Sgl Carbon Ag | Cathode system for electrolytic aluminum extraction |
CN2892888Y (en) * | 2006-03-20 | 2007-04-25 | 贵阳铝镁设计研究院 | Steel bar structure for improving aluminium electrolytic cell cathode current density |
PL1845174T3 (en) * | 2006-04-13 | 2011-10-31 | Sgl Carbon Se | Cathodes for aluminium electrolysis cell with non-planar slot design |
AU2012309834B2 (en) * | 2011-09-12 | 2014-10-30 | Alcoa Usa Corp. | Aluminum electrolysis cell with compression device and method |
CN202246908U (en) * | 2011-09-23 | 2012-05-30 | 高伟 | Copper bearing steel composite construction cathode steel bar |
GB2536901A (en) * | 2015-03-30 | 2016-10-05 | Dubai Aluminium Pjsc | Cathode block for electrolytic cell suitable for the Hall-Héroult process |
CN105671592B (en) * | 2016-03-14 | 2018-08-03 | 中冶天工集团有限公司 | Method for equally dividing cathode steel bar of aluminum electrolytic cell |
-
2017
- 2017-01-23 GB GB1701067.9A patent/GB2558936A/en not_active Withdrawn
-
2018
- 2018-01-18 WO PCT/IB2018/050300 patent/WO2018134754A1/en active Application Filing
- 2018-01-18 EP EP18741304.2A patent/EP3571333B1/en active Active
- 2018-01-18 CA CA3049822A patent/CA3049822C/en active Active
- 2018-01-18 PL PL18741304T patent/PL3571333T3/en unknown
Also Published As
Publication number | Publication date |
---|---|
CA3049822C (en) | 2024-03-26 |
EP3571333A1 (en) | 2019-11-27 |
EP3571333A4 (en) | 2020-09-09 |
WO2018134754A1 (en) | 2018-07-26 |
CA3049822A1 (en) | 2018-07-26 |
GB201701067D0 (en) | 2017-03-08 |
PL3571333T3 (en) | 2021-12-27 |
GB2558936A (en) | 2018-07-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP1146146B1 (en) | Horizontal drained cathode surface with recessed grooves for aluminium electrowinning | |
EP3571333B1 (en) | Cathode assembly with metallic collector bar for electrolytic cell suitable for the hall-héroult process | |
US7618519B2 (en) | Cathode element for use in an electrolytic cell intended for production of aluminum | |
US8628646B2 (en) | Grooved anode for electrolysis cell | |
EP1927679B1 (en) | Electrolysis cell for the production of aluminium comprising means to reduce the voltage drop | |
EP3277864B1 (en) | Cathode block for electrolytic cell suitable for the hall-héroult process | |
CA2347858C (en) | Cathode collector bar with spacer for improved heat balance | |
US5597461A (en) | Method of manufacturing an anode bar from a metal sleeve, a metal rod and a metal ring | |
EP3347509B1 (en) | Cathode assembly for electrolytic cell suitable for the hall-héroult process | |
EP3523463B1 (en) | Cathode assembly for electrolytic cell suitable for the hall-héroult process | |
WO2021240353A1 (en) | Cathode assembly with metallic collector bar systems for electrolytic cell suitable for the hall-héroult process | |
WO2016088001A1 (en) | Electrolytic pot for hall-heroult process, having a cathode formed of high and low cathode blocks | |
EP4394089A1 (en) | Cathode collector bar and cathode assembly for hall-heroult process with low voltage drop and low thermal loss | |
JPS5741393A (en) | Electrolytic furnace for production of aluminum | |
US20040016639A1 (en) | Interlocking wettable ceramic tiles | |
WO2017168310A1 (en) | Cathode block with copper-aluminium insert for electrolytic cell suitable for the hall-héroult process | |
CA2354120C (en) | Aluminium electrowinning cell with improved carbon cathode blocks | |
EP0613504B1 (en) | Cell for the electrolysis of alumina preferably at low temperatures | |
AU6551901A (en) | Horizontal drained cathode surface with recessed grooves for aluminium electrowinning | |
CN114182303A (en) | Electrolytic cell, in particular for the production of aluminium |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE |
|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE |
|
17P | Request for examination filed |
Effective date: 20190823 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
AX | Request for extension of the european patent |
Extension state: BA ME |
|
DAV | Request for validation of the european patent (deleted) | ||
DAX | Request for extension of the european patent (deleted) | ||
A4 | Supplementary search report drawn up and despatched |
Effective date: 20200810 |
|
RIC1 | Information provided on ipc code assigned before grant |
Ipc: C25C 3/16 20060101ALI20200804BHEP Ipc: C25C 3/08 20060101AFI20200804BHEP |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R079 Ref document number: 602018022075 Country of ref document: DE Free format text: PREVIOUS MAIN CLASS: C25C0003060000 Ipc: C25C0003080000 |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
RIC1 | Information provided on ipc code assigned before grant |
Ipc: C25C 3/16 20060101ALI20210409BHEP Ipc: C25C 3/08 20060101AFI20210409BHEP |
|
INTG | Intention to grant announced |
Effective date: 20210510 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE PATENT HAS BEEN GRANTED |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 602018022075 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D Ref country code: AT Ref legal event code: REF Ref document number: 1421719 Country of ref document: AT Kind code of ref document: T Effective date: 20210915 |
|
REG | Reference to a national code |
Ref country code: NO Ref legal event code: T2 Effective date: 20210818 |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG9D |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: MP Effective date: 20210818 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MK05 Ref document number: 1421719 Country of ref document: AT Kind code of ref document: T Effective date: 20210818 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: RS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211118 Ref country code: AT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211220 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20211119 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602018022075 Country of ref document: DE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SM Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: AL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed |
Effective date: 20220519 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
REG | Reference to a national code |
Ref country code: BE Ref legal event code: MM Effective date: 20220131 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220118 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220131 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220131 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220131 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20220118 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: PL Payment date: 20231222 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IS Payment date: 20240130 Year of fee payment: 7 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20240228 Year of fee payment: 7 Ref country code: GB Payment date: 20240111 Year of fee payment: 7 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: HU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO Effective date: 20180118 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NO Payment date: 20240130 Year of fee payment: 7 Ref country code: FR Payment date: 20240119 Year of fee payment: 7 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20210818 |