AU2003261034A1 - A material for structural components of an electrowinning cell for production of metal - Google Patents

A material for structural components of an electrowinning cell for production of metal Download PDF

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Publication number
AU2003261034A1
AU2003261034A1 AU2003261034A AU2003261034A AU2003261034A1 AU 2003261034 A1 AU2003261034 A1 AU 2003261034A1 AU 2003261034 A AU2003261034 A AU 2003261034A AU 2003261034 A AU2003261034 A AU 2003261034A AU 2003261034 A1 AU2003261034 A1 AU 2003261034A1
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essentially
elements
aluminium
sample
cell
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AU2003261034A
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Stein Julsrud
Tyke Naas
Turid Risdal
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Norsk Hydro ASA
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Norsk Hydro ASA
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/06Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
    • C25C3/08Cell construction, e.g. bottoms, walls, cathodes
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/06Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
    • C25C3/08Cell construction, e.g. bottoms, walls, cathodes
    • C25C3/12Anodes

Description

WO 2004/018738 PCT/N02003/000278 1 A material for structural components of an electrowinning cell for production of metal Field of Invention The present invention relates to a material that can be used for structural components in a cell for the electrolysis of alumina dissolved in a fluoride containing molten salt bath 5 by the use of essentially inert electrodes. Background Art Conventionally, aluminium is produced by the electrolysis of alumina dissolved in a cryolite based molten salt bath by the more than hundred years old Hall-Heroult process. In this process carbon electrodes are used, where the carbon anode is taking part in the 10 cell reaction resulting in the simultaneous production of CO 2 . The gross consumption of the anode is up to 550 kg/tonne of aluminium produced, causing emissions of green house gases like fluorocarbon compounds in addition to CO 2 . For both cost and environ mental reasons the replacement of carbon anodes with an effectively inert material would be highly advantageous. The electrolysis cell would then produce oxygen and 15 aluminium. An earlier, not yet disclosed Norwegian patent application No. 2001-0927 describes the development and design of a novel electrowinning cell for aluminium production. The novel cell is based on vertical electrode technology and a two chamber electrolysis cell 20 for separation of produced metal and evolved oxygen gas. The cell concept requires that certain structural elements are made of materials that must fulfil their functional require ments at elevated temperatures in an environment of a molten fluoride-based electrolyte. In some regions of the cell an additional requirement is that the materials must fulfil their functional requirements in contact with liquid aluminium, while in other regions 25 the materials must fulfil their functional requirements in contact with pure oxygen gas at a pressure of about one bar. Object of the Invention The object of the present invention is to identify a material that is stable at an oxygen partial pressure of 1 bar at temperatures above about 680'C and has a sufficiently low 30 solubility in the electrolyte to be used as a material for structural cell components in WO 2004/018738 PCT/N020031000278 2 oxidizing regions of an aluminium electrowinning cell based on substantially inert electrodes. Summary of the Invention The invention is the conclusion of an extensive search for materials capable of fulfilling 5 the requirements for a material for structural cell components in oxidizing regions of an aluminium electrowinning cell based on substantially inert electrodes. The stability requirements of such a material are similar to those of an inert anode in said electrowin ning cell. In the not yet published Norwegian Patent Application No. 2001-0928 the choice of possible element oxides for an inert anode is narrowed to: TiO 2 , Cr 2 0 3 , Fe 2
O
3 , 10 Mn 2
O
3 , CoO, NiO, CuO, ZnO, A1 2 0 3 , Ga 2
O
3 , ZrO 2 , SnO 2 and Hf0 2 . The main require ments for a material intended for use in structural cell components are stability at I bar oxygen pressure at temperatures above 680'C and a low solubility in the molten electro lyte. The electrical properties are less important, but its electrical conductivity should be far less that the electrical conductivity of the electrodes and the electrolyte. The material 15 should either itself fulfil the requirements, or it should upon contact with the molten electrolyte react to form a surface layer of an aluminate that fulfils the said requirements. Based on solubility considerations, CuO, Ga 2
O
3 , ZrO 2 and HfO 2 are elimi nated from the list of possible element oxides, and we are left with: TiO 2 , Cr 2 0 3 , Fe 2
O
3 , Mn 2
O
3 , CoO, NiO, ZnO, A1 2 0 3 , and SnO 2 . 20 The evaluation leads to three groups of materials: The first group comprises mixed oxides of the spinel structure with composition (AL A"u),(BiB",),(C'mC",),04, in which A' and A" are divalent elements , i. e., Co, Ni, 25 or Zn, B' and B" are trivalent elements, i. e., Al, Cr, Mn, or Fe and C' and C" are tetrava lent elements, i. e., Ti or Sn. 0 is the element oxygen. 0<u<1, 0<v<1, 0sw<1 1 x<2, Osy 2 and 0 zs1, x+y+z = 3 and 2x+3y+4z = 8. The second group comprises mixed oxides of the ilmenite structure with composition 30 A',-,A",TiO 3 , in which A' and A" are divalent elements, i. e., Co, Ni, or Zn. 0 is the element oxygen. 0 s<1.
WO 2004/018738 PCT/N02003/000278 3 The third group comprises the divalent oxides of Co, Ni and Zn or solid solutions of these. These will react with dissolved alumina to form surface layers of essentially insoluble aluminates. These materials may be expressed by the formula A' 4 A"(0. 0<t< . 5 Detailed Description of the Invention A material suitable as an essentially inert material for structural components in the oxidizing regions of a cell for the electrolytic production of aluminium from alumina dissolved in an essentially fluoride based electrolyte where cryolite is an important ingredient, must be resistant to oxidation and dissolution in the electrolyte. A selection 10 of the element oxides which a material for structural components can consist of, was performed based on the following criteria: -not a gas or having a high vapour pressure at process temperature -not converted by cryolite or A1F 3 in the cryolitic mixture, i.e. a large positive value of 15 AGO for the reaction between the element oxide and AIF 3 to form the element fluoride and aluminium oxide (reaction 1). MO, + 2x/3AF 3 = MiF 2 2x/6Al 2
O
3 (1) -not converted by alumina, i.e. not a negative value of AG" for the reaction between the element oxide aluminium oxide and sodium fluoride to form a sodium element 20 oxide and aluminium fluoride (reaction 2) MO, + 6yNaF + yA1 2
O
3 = Na 6 yMO.+3, + 2yAIF 3 (2) Of elements with the normal valence 2, the only possible elements are thus Co, Ni, Cu and Zn. Of elements with valence 3 one is left with only the elements Cr, Mn, Fe, Ga 25 and Al. Of elements with valence 4 one is left with only the elements Ti, Zr, Hf, Ge and Sn. Cu, Ga, Zr, Hf and Ge may be eliminated from the list based on solubility considera tions, and we are left with the following list of elements: Co, Ni, Zn, Al, Cr, Mn, Fe, Ti and Sn. The possible materials for structural cell components in an aluminium electrow inning cell based on substantially inert electrodes are thus limited to the oxides of the 30 listed elements, or combinations of these oxides in mixed oxide compounds. Under favourable conditions the divalent oxides NiO, CoO and ZnO all react with alumina to form an essentially insoluble surface aluminate layer (reaction 3).
WO 2004/018738 PCT/N02003/000278 4 AO(s) + A1 2 0 3 (diss) = AA1 2 0 4 (s) (3) where A = Co, Ni, Zn. Therefore, CoO, NiO and ZnO and solid solutions of these form one group of possible materials for structural cell components. expressed by the formula
A
1 -A",O. Ost<1 . This is further illustrated in Examples I and 2. 5 Compounds of di- and trivalent element oxides will in this case be of the spinel structure. Spinels like NiFe 2 0 4 , CoFe 2 0 4 , NiCr 2
O
4 and CoCr 2 0 4 have been suggested and extensively tested as candidates for inert anodes. In these materials, Al from the molten electrolyte has been observed to exchange with the trivalent cation to form 10 essentially insoluble, insulating solid solutions of the type Ni(B'Al,) 2 0 4 , where 0<v<1, B'= Fe, Cr, Mn. This is further illustrated in Examples 3, 4, and 6. These materials are thus possible materials for structural cell components. The pure aluminates NiA20 4 , CoAl20 4 and ZnAl 2
O
4 are also possible materials for structural cell components. 15 One compound of di- and tetravalent element oxides, Zn 2 SnO 4 , forms a spinel oxide. This material may in principle be used for structural cell components. Other stable spinel compositions that are possible materials for structural components of an aluminium electrowinning cell are achieved by substituting a divalent/trivalent spinel 20 with a tetravalent oxide, while simultaneously adjusting the contents of the divalent and trivalent oxides in order to maintain the site and charge balance requirements of the spinel structure. An embodiment of this invention is exemplified in Example 5. Spinel type materials thus form the second group of materials for structural components 25 of aluminium electrowinning cells. The possible spinels according to the present inven tion are given by the formula (A'-A"u),(B1B",)y(C'_C".),04, in which A' and A" are divalent elements , i. e., Co, Ni, or Zn, B' and B" are trivalent elements, i. e., Al, Cr, Mn, or Fe, and C' and C" are tetravalent elements, i. e., Ti or Sn. Ou<1, 0<v<1, 0sw<1 1Jx 2, 0sy 2 and 05z1, x+y+z = 3 and 2x+3y+4z = 8. 30 Another group of materials for structural components of aluminium electrowinning cells comprise the ilmenite type materials, NiTiO 3 , CoTiO 3 and solid solutions of these. These compositions are given by the formula A's,_A",TiO 3 , in which A' and A" are divalent elements, i. e., Co, Ni, or Zn. 0 is the element oxygen. 0 s<1.
WO 2004/018738 PCT/N02003/000278 5 The invention shall in the following be further described by figures and examples where: 5 Figure 1: Shows a photograph of a sample of a material for structural components in an electrolysis cell before and after the stability test of Example 3. Figure 2: Shows a backscatter SEM photograph of the reaction zone of a Ni 1 .Cr 2
O
4 material after 50 hours of exposure to molten fluoride electrolyte under anodic polarization. 10 Figure 3: Shows a backscatter SEM photograph of a NiFeCO 4 sample after 50 hours of exposure to molten fluoride electrolyte under anodic polarization. Figure 4: Shows a backscatter SEM photograph of a sample of Ni.,,"FeTio.s5x0 4 after the stability test of Example 5. Figure 5: Shows a backscatter SEM photograph of a Ni 101 Fe 2
O
4 sample after 30 hours 15 of exposure to molten fluoride electrolyte under anodic polarization. Example 1: Test of the stability of a NiO sample anodically polarized in a molten fluoride electrolyte. 20 A cermet with 75 wt% NiO and 25 wt% Ni was prepared using INCO Ni powder type 210, and NiO from Merck, Darmstadt. The material was sintered in argon atmosphere at 1400'C for 30 min. The sample was exposed to a molten fluoride bath under anodic polarization in order to 25 ensure a partial pressure of I bar oxygen on the sample surface. The electrolyte was contained in an alumina crucible with inner diameter 80 mm and height 150 mm. An outer alumina container with height 200 mm was used for safety, and the cell was covered with a lid made from high alumina cement. In the bottom of the crucible a 5 mm thick TiB 2 disc was placed, which made the liquid aluminium cathode stay horizon 30 tal. The electrical connection to the cathode was provided by a TiB 2 rod supported by an alumina tube to avoid oxidation. A platinum wire provided electrical connection to the TiB 2 cathode rod. A Ni wire provided for the electrical connection to the anode. The Ni wire and the anode above the electrolyte bath was masked with an alumina tube and alumina cement to prevent oxidation.
WO 2004/018738 PCT/N020031000278 6 340 g Al, (99.9% pure), from Hydro Aluminium was placed on the TiB 2 disc at the bottom of the alumina crucible. 5 The electrolyte was made by adding to the alumina crucible a mixture of: 532 g Na 3
AIF
6 (Greenland cryolite) 105 g AlF 3 (from Norzink, with about 10 % A1 2 0 3 ) 35 g Al 2 0 3 (annealed at 1200"C for some hours) 21 g CaF 2 (Fluka p.a.) 10 The sample of the material for structural cell components was suspended above the electrolyte during heating of the cell. The temperature was maintained at 970 0 C during the whole experiment. The sample of the material for structural cell components was lowered into the molten electrolyte and polarized anodically with a current density of 15 750 mA/cm 2 based on the bottom end cross sectional area of the sample. The real current density was somewhat lower because the side surfaces of the anode were also dipped into in the electrolyte. The experiment lasted for 8 hours. XRD (X-ray diffraction) analysis of the anode after 20 the experiment showed that the Ni metal was oxidized to NiO and the anode material was covered by an dense, protective, insulating layer of NiAl20 4 . Example 2: Test of the stability of a ZnO sample anodically polarized in a molten fluoride 25 electrolyte. ZnO was doped with 0.5 mol% A10 1
.
5 . Two Pt wires were pressed into the material in the longitudinal axis of the ZnO anode and acted as electrical conductors. The material was sintered at 1300'C for 1 hour. 30 The stability test was performed in the same manner as described in Example 1. The amounts of electrolyte and aluminium were the same. The temperature was 970'C. The current density was set to 1000 mA/cm 2 based on the bottom end cross sectional area of the sample The electrolysis experiment lasted for 24 hours. XRD (X-ray diffraction) WO 2004/018738 PCT/N02003/000278 7 analysis of the sample after the electrolysis experiment showed that ZnO had been converted to ZnA 2
O
4 during electrolysis. Example 3: 5 Test of the stability of a Nil 1 +Cr 2 0 4 sample anodically polarized in a molten fluoride electrolyte. The starting powder was prepared by a soft chemistry route. The appropriate amounts of Ni(N0 3
)
2 , and Cr(NO 3 )3 were complexed with citric acid in dilute nitric acid. After evaporation of excess water, the mixture was pyrolysed and calcined at 900'C for 10 10 hours. The sample was cold isostatically pressed at 200 MPa, then sintered at 1440'C for 3 hours. The material was found by XRD to possess the spinel structure. The stability test was performed in the same manner as described in Example 1, but a platinum wire provided electrical connection to the sample. The platinum wire to the 15 sample was protected by a 5 mm alumina tube. When the electrolysis started the anode was dipped approximately 1 cm into the electrolyte. A photograph of the sample before and after electrolysis is shown in Figure 1. The electrolyte, temperature and current density were the same as described in Example 20 2. The stability test lasted for 50 hours. After the experiment the sample was cut, polished and examined in SEM (Scanning Electron Microscope). A reaction zone could be seen between the Ni 1 1 Cr 2 0 4 - material and the electrolyte. Figure 2 shows the backscatter 25 SEM photograph of the reaction zone. On the photograph one can see a reaction zone that has propagated along the grain boundaries of the Nia.
1 Cr 2
O
4 material. The white particles are NiO. In the table below the relative EDS analysis results are reported. Ni, Cr, Al, and 0 were 30 the only elements detected. The aluminium present in the interior of the grains might be due to the preparation of the sample for analysis. Relative comparison between the elements Ni, Cr and Al: WO 2004/018738 PCT/N02003/000278 8 Element: Atom % in the centre of the grains Atom % in the reaction zone in in Figure 2: grain boundaries in Figure 2: Ni 33 47 Cr 66 8 Al 1 45 The SEM analysis shows that the reaction product consisted of a material where the chromium atoms were partly exchanged with aluminium atoms as described by the 5 formula NiCr 2 .4Alx0 4 where x varies from 0 to 2. The reaction product forms an insulat ing coating. Example 4: Test of the stability of a NiFcCrO 4 sample anodically polarized in a molten fluoride 10 electrolyte. The starting powder was prepared by a soft chemistry route. The appropriate amounts of Ni(N0 3
)
2 , Fe(N0 3
)
3 and Cr(N0 3
)
3 were complexed with citric acid in dilute nitric acid. After evaporation of excess water, the mixture was pyrolysed and calcined at 900'C for 10 hours. The sample was cold isostatically pressed at 200 MPa, then sintered at 1600'C 15 for 3 hours. The material was found by XRD to possess the spinel structure. The stability test was performed in the same manner as described in Example 3. The amounts of electrolyte and aluminium were the same. The current density was set to 1000 mA/cm 2 based on the cross sectional area of the rectangular sample. The experi 20 ment lasted for 50 hours. Examinaton of the sample after exposure to molten fluorides under anodic polarization showed a several micron thick reaction layer where Cr in the material was partly exchanged with Al atoms. A backscatter SEM photograph of the reaction layer is shown in Figure 3. Light grey areas consist of original NiFeCrO 4 material. Medium grey area contains almost no Cr atoms and a much lower content of 25 Fe. EDS analysis of the medium grey reaction layer shown in Fig. 3 compared to original NiFeCrO 4 material and the inner of the anode light grey area also shown in Fig. 3 are summarized in table below. The only elements detected were Ni, Cr, Fe, Al and 0. 30 Comparison of the relative amounts of Cr, Fe, Ni and Al: WO 2004/018738 PCT/N020031000278 9 Element: Atom % in the original NiFeCrO 4 Atom % in the reaction layer after material. Light grey area in Fig. 3. the test. Medium grey area in Fig. 3. Cr 33.3 0 Fe 33.3 16 Ni 33.3 35 Al 0 49 The conclusion of the stability test is that the NiFeCFO material reacts with alumina in the electrolyte and forms a dense, essentially insoluble, insulating layer of 5 NiFei.-Al 1 +x0 4 . Example 5: Test of the stability of a Ni.5,FeTiO.s.20 4 sample anodically polarized in a molten fluoride electrolyte. 10 The starting powder was prepared by a soft chemistry route. The appropriate amounts of Ni(N0 3
)
2 , Fe(N0 3
)
3 and TiO 5
H
1 4 Cio (titanyl acetylacetonate) were complexed with citric acid in dilute nitric acid. After evaporation of excess water, the mixture was pyrolysed and calcined at 900'C for 10 hours. The sample was cold isostatically pressed at 200 MPa, then sintered at 1500'C for 3 hours. The material was found by XRD to possess 15 the spinel structure. The stability test was performed in the same manner as described in Example 3. The amounts of electrolyte and aluminium were the same. The current density was set to 1000 mA/cm 2 based on the cross sectional area of the rectangular sample. The experi 20 ment lasted for 30 hours. After the experiment the sample was cut, polished and examined in SEM. The backscatter photo in Fig. 4 shows the end of the sample facing the cathode. In this experiment no reaction layer was detected on the Nii.
5 +XFeTio.5-xO4 anode after 30 hours. 25 Example 6: Test of the stability of a Nii.oFe 2
O
4 sample anodically polarized in a molten fluoride electrolyte. The starting powder was prepared by a soft chemistry route. The appropriate amounts of Ni(NO 3
)
2 , and Fe(N0 3
)
3 were complexed with citric acid in dilute nitric acid. After 30 evaporation of excess water, the mixture was pyrolysed and calcined at 900 0 C for 10 hours. The sample was cold isostatically pressed at 200 MPa, then sintered at 1450*C for 3 hours. The material was found by XRD to possess the spinel structure.
WO 2004/018738 PCT/N02003/000278 10 The stability test was performed in the same manner as described in Example 3. The amounts of electrolyte and aluminium were the same. The current density was -set to 1000 mA/cm 2 based on the cross sectional area of the rectangular anode. The experi 5 ment was stopped after 30 hours. After the experiment the sample was cut, polished and examined in SEM. Figure 5 shows a backscatter photograph of the sample at the end facing the cathode. An approximately 10 micron thick reaction layer is seen. A line scan EDS analysis was done to examine whether the layer was a reaction layer or 10 electrolyte adhering to the surface. The line scan indicated a thin layer of bath compo nents, and then a reaction layer of approximately 10 micron thickness. In the interior of the anode and in the reaction layer only oxygen was detected in addition to Ni, Fe and Al. The results are reported in the table below: 15 Comparison of the relative amounts of Ni, Fe and Al: Element: Atom % of element in the interior of Atom % of element in the reaction the anode shown in Figure 5 and layer as shown in Figure 5 and analysed with line scan EDS: analysed with line scan EDS: Ni 33 30 Fe 67 30 Al 0 40 20 In the 10 micron thick reaction layer the iron atoms were partly exchanged with alumin ium atoms to form an essentially insoluble, insulating layer of NiFe 2 ._Alx0 4 . 1

Claims (10)

1. A material suitable for manufacture of structural components in a cell for electrolytic reduction of alumina to aluminium, 5 characterisedby the formula (A',uA"u),(B'I-B",)y(C'j.,C",)z0 4 , in which A' and A" are divalent elements from the group Co, Ni, or Zn, B' and B" are trivalent elements from the group Al, Cr, Mn, or Fe and C' and C" are the tetravalent elements Ti or Sn, 0 is the element oxygen, 0:u<1, 0<v<1, 0<w<1 I1x 2, Ofy 2 and 0 z1, x+y+z = 3 and 2x+3y+4z = 8. 10
2. A material suitable for manufacture of structural components in a cell for electrolytic reduction of alumina to aluminium, c h a r a c t e r i s e d by the formula A' 1 .A"sTiO 3 , in which A' and A" are divalent elements from the group Co, 15 Ni, or Zn and 0 is the element oxygen. O:s<1.
3. A material suitable for manufacture of structural components in a cell for electrolytic reduction of alumina to aluminium, c h a r a c t e r i s e d by 20 the formula A' 11 A",O, in which A' and A" are divalent elements from the group Co, Ni, or Zn and 0 is the element oxygen. Ost<1.
4. A material in accordance with claim 1, c h a r a c t e r i s e d in that 25 the cation A' is essentially divalent Ni, u is essentially 0 and x is essentially 1.
5. A material in accordance with claim 1, c h a r a c t e r i s e d in that the cation B' is essentially trivalent Al, the cation B" is essentially trivalent Fe and y is 30 essentially 2. WO 2004/018738 PCT/N02003/000278 12
6. A material in accordance with claim 2, c h a r a c t e r i s e d i n that the cation A' is essentially divalent Ni, s is essentially 0, and the cation B' is essentially 5 tetravalent Ti.
7. A material suitable for manufacture of structural components in a cell for electrolytic reduction of alumina to aluminium, c h a r a c t e r i s e d in a first embodiment by 10 the formula (A' 1 .,A"e)x(B' 1 -B",)y(C' 1 .C".),O 4 , or in a second embodiment by the formula A' 1 sA"sTiO 3 , or in a third embodiment by the formula A' 1 tA",O, 15 in which A' and A" are divalent elements from the group Co, Ni, or Zn, B' and B" are trivalent elements from the group Al, Cr, Mn, or Fe and C' and C" are the tetravalent elements Ti or Sn, 0 is the element oxygen, 05s<1, 0<t<1, Osu<t, Osv<1, 0sw<1 1 x 2, 05y 2 and O z1 1, x+y+z = 3 and 2x+3y+4z = 8. 20
8. A material in accordance with claim 7, ch aracteri sed in that in the first embodiment of the invention the cation A' is essentially divalent Ni, u is essentially 0 and x is essentially 1. 25
9. A material in accordance with claim 7, ch aracteri sed in that in the first embodiment of the invention the cation B' is essentially trivalent Al, the cation B" is essentially trivalent Fe and y is essentially 2. 30
10. A material in accordance with claim 7, c h a r a c t e r i s e d in that in the second embodiment of the invention the cation A' is essentially divalent Ni and s is essentially 0.
AU2003261034A 2002-08-23 2003-08-15 A material for structural components of an electrowinning cell for production of metal Abandoned AU2003261034A1 (en)

Applications Claiming Priority (3)

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NO20024049 2002-08-23
NO20024049A NO20024049D0 (en) 2002-08-23 2002-08-23 Material for use in an electrolytic cell
PCT/NO2003/000278 WO2004018738A1 (en) 2002-08-23 2003-08-15 A material for structural components of an electrowinning cell for production of metal

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CA (1) CA2496518A1 (en)
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US8594417B2 (en) * 2007-11-27 2013-11-26 Alcoa Inc. Systems and methods for inspecting anodes and smelting management relating to the same
JP2017057426A (en) * 2015-09-14 2017-03-23 Tdk株式会社 Method for producing electrode for electrolysis

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US4075070A (en) * 1976-06-09 1978-02-21 Ppg Industries, Inc. Electrode material
CH642402A5 (en) * 1979-12-18 1984-04-13 Alusuisse ANODE OF DIMENSIONAL STABLE OXIDE CERAMIC INDIVIDUAL ELEMENTS.
US4357226A (en) * 1979-12-18 1982-11-02 Swiss Aluminium Ltd. Anode of dimensionally stable oxide-ceramic individual elements
JPH05101907A (en) * 1991-03-30 1993-04-23 Toshiba Corp Breaker for electric power and resistor for electric power
US5482907A (en) * 1994-05-26 1996-01-09 National Science Council Ceramic composite containing a spinel phase and an oxide phase and the preparation thereof
US6821312B2 (en) * 1997-06-26 2004-11-23 Alcoa Inc. Cermet inert anode materials and method of making same
US5865980A (en) * 1997-06-26 1999-02-02 Aluminum Company Of America Electrolysis with a inert electrode containing a ferrite, copper and silver
US6423204B1 (en) * 1997-06-26 2002-07-23 Alcoa Inc. For cermet inert anode containing oxide and metal phases useful for the electrolytic production of metals
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JP5072136B2 (en) * 1998-07-24 2012-11-14 千代田化工建設株式会社 Method for producing porous spinel complex oxide
JP3928309B2 (en) * 1998-10-06 2007-06-13 昭栄化学工業株式会社 Nickel composite particles, conductor paste, and ceramic multilayer electronic components
US7014881B2 (en) * 1999-11-01 2006-03-21 Alcoa Inc. Synthesis of multi-element oxides useful for inert anode applications
NO20010928D0 (en) * 2001-02-23 2001-02-23 Norsk Hydro As Material for use in production
US7033469B2 (en) * 2002-11-08 2006-04-25 Alcoa Inc. Stable inert anodes including an oxide of nickel, iron and aluminum

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NO20024049D0 (en) 2002-08-23
CN1688751A (en) 2005-10-26
IS7760A (en) 2005-03-21
US20070289866A1 (en) 2007-12-20
WO2004018738A1 (en) 2004-03-04
EP1543179A1 (en) 2005-06-22
ZA200501560B (en) 2005-09-06
CA2496518A1 (en) 2004-03-04

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