WO2004018738A1 - 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
WO2004018738A1
WO2004018738A1 PCT/NO2003/000278 NO0300278W WO2004018738A1 WO 2004018738 A1 WO2004018738 A1 WO 2004018738A1 NO 0300278 W NO0300278 W NO 0300278W WO 2004018738 A1 WO2004018738 A1 WO 2004018738A1
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essentially
elements
aluminium
cell
sample
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PCT/NO2003/000278
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French (fr)
Inventor
Tyke Naas
Turid Risdal
Stein Julsrud
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Norsk Hydro Asa
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Priority to EA200500396A priority Critical patent/EA200500396A1/en
Priority to CA002496518A priority patent/CA2496518A1/en
Priority to US10/525,405 priority patent/US20050224362A1/en
Priority to AU2003261034A priority patent/AU2003261034A1/en
Priority to EP03792888A priority patent/EP1543179A1/en
Priority to BR0313715-5A priority patent/BR0313715A/en
Priority to JP2004530669A priority patent/JP2005536636A/en
Publication of WO2004018738A1 publication Critical patent/WO2004018738A1/en
Priority to IS7760A priority patent/IS7760A/en
Priority to US11/892,106 priority patent/US20070289866A1/en

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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

Definitions

  • 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 by the use of essentially inert electrodes.
  • 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.
  • carbon electrodes are used, where the carbon anode is taking part in the 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 greenhouse gases like fluorocarbon compounds in addition to CO 2 .
  • the electrolysis cell would then produce oxygen and aluminium.
  • 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 solubility in the electrolyte to be used as a material for structural cell components in oxidizing regions of an aluminium electrowinning cell based on substantially inert electrodes.
  • the invention is the conclusion of an extensive search for materials capable of fulfilling 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 electrowinning cell.
  • the choice of possible element oxides for an inert anode is narrowed to: TiO 2 , Cr 2 O 3 , Fe 2 O 3 , Mn 2 O 3 , CoO, NiO, CuO, ZnO, Al 2 O 3 , Ga 2 O 3 , ZrO 2 , SnO 2 and HfO 2 .
  • the main requirements for a material intended for use in structural cell components are stability at 1 bar oxygen pressure at temperatures above 680°C and a low solubility in the molten electrolyte.
  • 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 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.
  • CuO, Ga 2 O 3 , ZrO 2 and HfO 2 are eliminated from the list of possible element oxides, and we are left with: TiO 2 , Cr 2 O 3 , Fe 2 O 3 , Mn 2 O 3 , CoO, NiO, ZnO, Al 2 O 3 , and SnO 2 .
  • the first group comprises mixed oxides of the spinel structure with composition (AY u A" u ) x (By v B" v ) y (CVwC"w)- ⁇ 4, in which A' and A" are divalent elements , i. e., Co, Ni, or Zn, B' and B" are trivalent elements, . e., Al, Cr, Mn, or Fe and C and C" are tetrava- lent elements, i. e., Ti or Sn.
  • the second group comprises mixed oxides of the ilmenite structure with composition A' ⁇ . s A" s TiO 3 , in which A' and A" are divalent elements, i. e., Co, Ni, or Zn. O is the element oxygen. 0 ⁇ s ⁇ l.
  • 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 AY ⁇ A",0. 0 ⁇ t ⁇ l .
  • 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.
  • MO x + 2x/3AlF 3 MF 2x +2x/6Al 2 O 3 (1)
  • reaction 2 (reaction 2)
  • MO x + 6yNaF + yAl 2 O 3 Na ⁇ , y MO x+ 3 y + 2yAlF 3 (2)
  • elements with the normal valence 2 the only possible elements are thus Co, Ni, Cu and Zn.
  • elements with valence 3 one is left with only the elements Cr, Mn, Fe, Ga and Al.
  • 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 considerations, 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 electrowinning cell based on substantially inert electrodes are thus limited to the oxides of the listed elements, or combinations of these oxides in mixed oxide compounds.
  • 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 NiAl 2 O 4 , CoAI 2 0 and ZnAl 2 O 4 are also possible materials for structural cell components.
  • This material may in principle be used for structural cell components.
  • spinel type materials thus form the second group of materials for structural components of aluminium electrowinning cells.
  • Another group of materials for structural components of aluminium electrowinning cells comprise the ilmenite type materials, NiTiO 3 , C0T1O 3 and solid solutions of these. These compositions are given by the formula A' ⁇ . s A" s TiO 3 , in which A' and A" are divalent elements, i. e., Co, Ni, or Zn. O is the element oxygen. 0 ⁇ s ⁇ l.
  • A' and A" are divalent elements, i. e., Co, Ni, or Zn.
  • O is the element oxygen. 0 ⁇ s ⁇ l.
  • 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] ⁇ Cr 2 O 4 material after 50 hours of exposure to molten fluoride electrolyte under anodic polarization.
  • Figure 3 Shows a backscatter SEM photograph of a NiFeCrO 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 ⁇ 5+x FeTio 5 - x O 4 after the stability test of Example 5.
  • Figure 5 Shows a backscatter SEM photograph of a Ni ⁇ o ⁇ Fe 2 O 4 sample after 30 hours of exposure to molten fluoride electrolyte under anodic polarization.
  • the sample was exposed to a molten fluoride bath under anodic polarization in order to ensure a partial pressure of 1 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.
  • a 5 mm thick TiB 2 disc was placed, which made the liquid aluminium cathode stay horizon- 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.
  • 340 g Al, (99 9% pure), from Hydro Aluminium was placed on the T ⁇ B 2 disc at the bottom of the alumina crucible
  • the electiolyte was made by adding to the alumina crucible a mixture of 532 g Na-,A1F 6 (Gieenland cryolite) 105 g AIFj (from Norzink, with about 10 % Al 2 O 3 ) 35 g Al 2 O 3 (annealed at 1200°C for some hours) 21 g CaF 2 (Fluka p a )
  • the sample of the mate ⁇ al for structural cell components was suspended above the electrolyte du ⁇ ng heating of the cell The temperature was maintained at 970°C du ⁇ ng the whole expe ⁇ ment
  • the sample of the mate ⁇ al for structural cell components was lowered into the molten electrolyte and polarized anodically with a current density of 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
  • ZnO was doped with 0 5 mol% Aid s
  • Two Pt wires were pressed into the mate ⁇ al in the longitudinal axis of the ZnO anode and acted as elect ⁇ cal conductois
  • the mate ⁇ al was sintered at 1300°C for 1 hour
  • the stability test was performed in the same manner as descnbed 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 expe ⁇ ment lasted for 24 hours XRD (X-ray diffraction) analysis of the sample after the electrolysis experiment showed that ZnO had been converted to ZnAl 2 O 4 during electrolysis.
  • Example 3 Test of the stability of a Ni 1+x Cr 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 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 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 sample was protected by a 5 mm alumina tube.
  • 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 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[. ⁇ Cr 2 O 4 - material and the electrolyte.
  • Figure 2 shows the backscatter SEM photograph of the reaction zone. On the photograph one can see a reaction zone that has propagated along the grain boundaries of the NiuCr 2 O 4 material. The white particles are NiO.
  • reaction product consisted of a material where the chromium atoms were partly exchanged with aluminium atoms as described by the formula NiCr 2 . x Al x O 4 where x varies from 0 to 2.
  • the reaction product forms an insulating coating.
  • the starting powder was prepared by a soft chemistry route.
  • the appropriate amounts of Ni(NO 3 ) 2 , Fe(NO 3 ) 3 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 hours. The sample was cold isostatically pressed at 200 MPa, then sintered at 1600°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 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- 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 Fe.
  • NiFeCrO 4 material reacts with alumina in the electrolyte and forms a dense, essentially insoluble, insulating layer of NiFe,. x Al ⁇ +x O 4 .
  • Ni(NO 3 ) 2 , Fe(NO 3 ) 3 and TiOsH ⁇ 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 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- 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 Ni ⁇ . 5+x FeTio.5- ⁇ 4 anode after 30 hours.
  • the starting powder was prepared by a soft chemistry route.
  • the appropriate amounts of Ni(NO 3 ) 2 , and Fe(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 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.
  • the stability test was performed in the same manner as desc ⁇ bed in Example 3
  • the amounts of electrolyte and aluminium were the same
  • the current density was et to 1000 mA/cm 2 based on the cioss sectional area of the rectangular anode
  • the expe ⁇ - ment was stopped after 30 hours After the expe ⁇ ment the sample was cut, polished and examined in SEM Figuie 5 shows a backscatter photograph of the sample at the end facing the cathode An approximately 10 micron thick reaction layer is seen
  • 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:

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Abstract

A material suitable for use for structural components in a cell for the electrolytic reduction of alumina to aluminium metal defined either by: • the formula (A'l-uA'u)x(B'l-vB'v)y(C'l-wC'w)zO4, 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. O is the element oxygen. 0≤ u<1, 0≤ v<1, 0≤ w<1 1≤ x ≤2, 0 ≤ y ≤ 2 and 0≤ z ≤1, x+y+z = 3 and 2x+3y+4z = 8, or • the formula A'1-SA'sTi03, in which A' and A' are divalent elements from the group Co, Ni, or Zn. O is the element oxygen. 0 ≤ s<1 or • the formula A'l-tA'tO, in which A' and A' are divalent elements from the group Co, Ni, or Zn. O is the element oxygen. 0 ≤ t<1.

Description

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 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 cell reaction resulting in the simultaneous production of CO2. The gross consumption of the anode is up to 550 kg/tonne of aluminium produced, causing emissions of greenhouse gases like fluorocarbon compounds in addition to CO2. For both cost and environmental reasons the replacement of carbon anodes with an effectively inert material would be highly advantageous. The electrolysis cell would then produce oxygen and 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 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 requirements 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 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 solubility in the electrolyte to be used as a material for structural cell components in 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 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 electrowinning 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: TiO2, Cr2O3, Fe2O3, Mn2O3, CoO, NiO, CuO, ZnO, Al2O3, Ga2O3, ZrO2, SnO2 and HfO2. The main requirements for a material intended for use in structural cell components are stability at 1 bar oxygen pressure at temperatures above 680°C and a low solubility in the molten electrolyte. 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 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, Ga2O3, ZrO2 and HfO2 are eliminated from the list of possible element oxides, and we are left with: TiO2, Cr2O3, Fe2O3, Mn2O3, CoO, NiO, ZnO, Al2O3, and SnO2.
The evaluation leads to three groups of materials:
The first group comprises mixed oxides of the spinel structure with composition (AYuA"u)x(ByvB"v)y(CVwC"w)-θ4, in which A' and A" are divalent elements , i. e., Co, Ni, or Zn, B' and B" are trivalent elements, . e., Al, Cr, Mn, or Fe and C and C" are tetrava- lent elements, i. e., Ti or Sn. O is the element oxygen. 0≤u<l, 0<v<l, 0<w<l l≤x<2, 0<y<2 and O≤z≤l, x+y+z = 3 and 2x+3y+4z = 8.
The second group comprises mixed oxides of the ilmenite structure with composition A'ι.sA"sTiO3, in which A' and A" are divalent elements, i. e., Co, Ni, or Zn. O is the element oxygen. 0<s<l. 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 AYιA",0. 0<t<l .
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 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 A1F3 in the cryolitic mixture, i.e. a large positive value of ΔG° for the reaction between the element oxide and A1F3 to form the element fluoride and aluminium oxide (reaction 1).
MOx + 2x/3AlF3 = MF2x+2x/6Al2O3 (1)
-not converted by alumina, i.e. not a negative value of ΔG° for the reaction between the element oxide aluminium oxide and sodium fluoride to form a sodium element oxide and aluminium fluoride (reaction 2)
MOx + 6yNaF + yAl2O3 = Na<,yMOx+3y + 2yAlF3 (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 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 considerations, 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 electrowinning cell based on substantially inert electrodes are thus limited to the oxides of the 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). AO(s) + Al2Oι (diss) = AAI2O4 (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'uA'Α 0<t<l . This is further illustrated in Examples 1 and 2.
Compounds of di- and trivalent element oxides will in this case be of the spinel structure. Spinels like NiFe O4, CoFe2O4, NiCr2O4 and CoCr2O4 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 essentially insoluble, insulating solid solutions of the type Ni(B'..vAlv)2O4, where 0<v<l,
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 NiAl2O4, CoAI20 and ZnAl2O4 are also possible materials for structural cell components.
One compound of di- and tetravalent element oxides, Zn2SnO4, 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 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 of aluminium electrowinning cells. The possible spinels according to the present invention are given by the formula (AYuA"u)x(B'ι.vB"v)y(CVwC"w)IO4, 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, . e., Ti or Sn. 0<u<l, 0<v<l, 0<w<l l<x<2, 0<y<2 and O≤z≤l, x+y+z = 3 and 2x+3y+4z = 8.
Another group of materials for structural components of aluminium electrowinning cells comprise the ilmenite type materials, NiTiO3, C0T1O3 and solid solutions of these. These compositions are given by the formula A'ι.sA"sTiO3, in which A' and A" are divalent elements, i. e., Co, Ni, or Zn. O is the element oxygen. 0<s<l. The invention shall in the following be further described by figures and examples where:
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] ιCr2O4 material after 50 hours of exposure to molten fluoride electrolyte under anodic polarization. Figure 3: Shows a backscatter SEM photograph of a NiFeCrO4 sample after 50 hours of exposure to molten fluoride electrolyte under anodic polarization.
Figure 4: Shows a backscatter SEM photograph of a sample of Niι 5+xFeTio5-xO4 after the stability test of Example 5.
Figure 5: Shows a backscatter SEM photograph of a Niι oιFe2O4 sample after 30 hours 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. 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 ensure a partial pressure of 1 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 TiB2 disc was placed, which made the liquid aluminium cathode stay horizon- tal. The electrical connection to the cathode was provided by a TiB2 rod supported by an alumina tube to avoid oxidation. A platinum wire provided electrical connection to the TiB2 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. 340 g Al, (99 9% pure), from Hydro Aluminium was placed on the TιB2 disc at the bottom of the alumina crucible
The electiolyte was made by adding to the alumina crucible a mixture of 532 g Na-,A1F6 (Gieenland cryolite) 105 g AIFj (from Norzink, with about 10 % Al2O3 ) 35 g Al2O3 (annealed at 1200°C for some hours) 21 g CaF2 (Fluka p a )
The sample of the mateπal for structural cell components was suspended above the electrolyte duπng heating of the cell The temperature was maintained at 970°C duπng the whole expeπment The sample of the mateπal for structural cell components was lowered into the molten electrolyte and polarized anodically with a current density of 750 mA/cm2 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 expeπment lasted for 8 hours XRD (X-ray diffraction) analysis of the anode after the expeπment showed that the Ni metal was oxidized to NiO and the anode mateπal was covered by an dense, protective, insulating layer of NιAl2O4
Example 2:
Test of the stability of a ZnO sample anodically polarized in a molten fluoride electrolyte.
ZnO was doped with 0 5 mol% Aid s Two Pt wires were pressed into the mateπal in the longitudinal axis of the ZnO anode and acted as electπcal conductois The mateπal was sintered at 1300°C for 1 hour
The stability test was performed in the same manner as descnbed 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/cm2 based on the bottom end cross sectional area of the sample The electrolysis expeπment lasted for 24 hours XRD (X-ray diffraction) analysis of the sample after the electrolysis experiment showed that ZnO had been converted to ZnAl2O4 during electrolysis.
Example 3: Test of the stability of a Ni1+xCr2O4 sample anodically polarized in a molten fluoride electrolyte.
The starting powder was prepared by a soft chemistry route. The appropriate amounts of Ni(NO3)2, and Cr(NO3)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 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 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 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[.ιCr2O4 - material and the electrolyte. Figure 2 shows the backscatter SEM photograph of the reaction zone. On the photograph one can see a reaction zone that has propagated along the grain boundaries of the NiuCr2O4 material. The white particles are NiO.
In the table below the relative EDS analysis results are reported. Ni, Cr, Al, and O were 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: 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 I 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 formula NiCr2.xAlxO4 where x varies from 0 to 2. The reaction product forms an insulating coating.
Example 4:
Test of the stability of a NiFeCrO4 sample anodically polarized in a molten fluoride electrolyte.
The starting powder was prepared by a soft chemistry route. The appropriate amounts of Ni(NO3)2, Fe(NO3)3 and Cr(NO3)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 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/cm2 based on the cross sectional area of the rectangular sample. The experi- 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 NiFeCrO4 material. Medium grey area contains almost no Cr atoms and a much lower content of Fe.
EDS analysis of the medium grey reaction layer shown in Fig. 3 compared to original NiFeCrO4 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 O.
Comparison of the relative amounts of Cr, Fe, Ni and Al: Element: Atom % in the original NiFeCrO4 Atom % in the reaction layer after material. Light grey area in Fig. 3. the test. Medium grey area in Fiσ f,
Cr 33.3 0 S
Fe 33.3 16
Ni 33.3 35
Al 0 49
The conclusion of the stability test is that the NiFeCrO4 material reacts with alumina in the electrolyte and forms a dense, essentially insoluble, insulating layer of NiFe,.xAlι+xO4.
Example 5:
Test of the stability of a Nij 5+χFeTi0.5-χO sample anodically polarized in a molten fluoride electrolyte. The starting powder was prepared by a soft chemistry route. The appropriate amounts of
Ni(NO3)2, Fe(NO3)3 and TiOsHμCio (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 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/cm2 based on the cross sectional area of the rectangular sample. The experi- 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 Niι.5+xFeTio.5-χθ4 anode after 30 hours.
Example 6:
Test of the stability of a Niι.oιFe2O4 sample anodically polarized in a molten fluoride electrolyte.
The starting powder was prepared by a soft chemistry route. The appropriate amounts of Ni(NO3)2, and Fe(NO3)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 1450°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 descπbed in Example 3 The amounts of electrolyte and aluminium were the same The current density was et to 1000 mA/cm2 based on the cioss sectional area of the rectangular anode The expeπ- ment was stopped after 30 hours After the expeπment the sample was cut, polished and examined in SEM Figuie 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 oi electrolyte adheπng to the surface The line scan indicated a thin layer of bath components, and then a reaction layer of approximately 10 micron thickness In the inteπor 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
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
In the 10 micron thick reaction layer the iron atoms were partly exchanged with aluminium atoms to form an essentially insoluble, insulating layer of NιFe2 xAlxO4

Claims

Claims
1. A material suitable for manufacture of structural components in a cell for electrolytic reduction of alumina to aluminium, characterised by the formula (A'ι-uA"u)x(BYvB"v)y(CYwC"w)*O4, 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, O is the element oxygen, 0<u<l, 0<v<l, 0<w<l l≤x<2, 0<y<2 and O≤z≤l, x+y+z = 3 and 2x+3y+4z = 8.
2. A material suitable for manufacture of structural components in a cell for electrolytic reduction of alumina to aluminium, characterised by the formula A'ι.sA"sTiO3, in which A' and A" are divalent elements from the group Co, Ni, or Zn and O is the element oxygen.0<s<l.
3. A material suitable for manufacture of structural components in a cell for electrolytic reduction of alumina to aluminium, characterised by the formula A' A",O, in which A' and A" are divalent elements from the group Co, Ni, or Zn and O is the element oxygen.0<t< 1.
4. A material in accordance with claim 1, characterised in that the cation A' is essentially divalent Ni, u is essentially 0 and x is essentially 1.
5. A material in accordance with claim 1, characterised in that the cation B' is essentially trivalent Al, the cation B" is essentially trivalent Fe and y is essentially 2. 6 A mateπal in accordance with claim 2, characteπsedin that the cation A' is essentially divalent Ni, s is essentially 0, and the cation B' is essentially tetravalent Ti
7 A mateπal suitable for manufacture of structural components in a cell for electrolytic reduction of alumina to aluminium, characterised in a first embodiment by the formula (A1,
Figure imgf000013_0001
wC"w)2O4, or in a second embodiment by the formula A\ sA"sTιO3, or m a third embodiment by the formula A\ tA",O, 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, O is the element oxygen, 0<s<l, 0<t<l, 0<u<l, 0<v<l, 0<w<l l<x<2, 0<y<2 and O≤z≤l, x+y+z = 3 and 2x+3y+4z = 8
8 A mateπal in accordance with claim 7, characterised 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
9 A mateπal in accordance with claim 7, characterised in that in the first embodiment of the invention the cation B' is essentially tπvalent Al, the cation B" is essentially tπvalent Fe and y is essentially 2
10 A mateπal in accordance with claim 7, characterised in that in the second embodiment of the invention the cation A' is essentially divalent Ni and s is essentially 0
PCT/NO2003/000278 2002-08-23 2003-08-15 A material for structural components of an electrowinning cell for production of metal WO2004018738A1 (en)

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EA200500396A EA200500396A1 (en) 2002-08-23 2003-08-15 MATERIAL FOR STRUCTURAL COMPONENTS OF ELECTROCHEMICAL CAMERA FOR METAL PRODUCTION
CA002496518A CA2496518A1 (en) 2002-08-23 2003-08-15 A material for structural components of an electrowinning cell for production of metal
US10/525,405 US20050224362A1 (en) 2002-08-23 2003-08-15 Material for structural components of an electrowinning cell for production of metal
AU2003261034A AU2003261034A1 (en) 2002-08-23 2003-08-15 A material for structural components of an electrowinning cell for production of metal
EP03792888A EP1543179A1 (en) 2002-08-23 2003-08-15 A material for structural components of an electrowinning cell for production of metal
BR0313715-5A BR0313715A (en) 2002-08-23 2003-08-15 Material for fabrication of structural components, excluding electrodes, in a cell for electrolytically reducing alumina to aluminum
JP2004530669A JP2005536636A (en) 2002-08-23 2003-08-15 Material of structural member of electrowinning tank for metal production
IS7760A IS7760A (en) 2002-08-23 2005-03-21 Materials in the construction of electrolytic metallurgy for producing metals
US11/892,106 US20070289866A1 (en) 2002-08-23 2007-08-20 Material for structural components of an electrowinning cell for production of metal

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090136122A1 (en) * 2007-11-27 2009-05-28 Alcoa Inc. Systems and methods for inspecting anodes and smelting management relating to the same

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017057426A (en) * 2015-09-14 2017-03-23 Tdk株式会社 Method for producing electrode for electrolysis

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2065708A (en) * 1979-12-18 1981-07-01 Alusuisse Anodes for electrolytic furnaces
US6113758A (en) * 1998-07-30 2000-09-05 Moltech Invent S.A. Porous non-carbon metal-based anodes for aluminium production cells
US6126799A (en) * 1997-06-26 2000-10-03 Alcoa Inc. Inert electrode containing metal oxides, copper and noble metal
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
WO2002066710A1 (en) * 2001-02-23 2002-08-29 Norsk Hydro Asa A material for a dimensionally stable anode for the electrowinning of aluminium

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4075070A (en) * 1976-06-09 1978-02-21 Ppg Industries, Inc. Electrode material
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
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
US7033469B2 (en) * 2002-11-08 2006-04-25 Alcoa Inc. Stable inert anodes including an oxide of nickel, iron and aluminum

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2065708A (en) * 1979-12-18 1981-07-01 Alusuisse Anodes for electrolytic furnaces
US6126799A (en) * 1997-06-26 2000-10-03 Alcoa Inc. Inert electrode containing metal oxides, copper and noble metal
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
US6113758A (en) * 1998-07-30 2000-09-05 Moltech Invent S.A. Porous non-carbon metal-based anodes for aluminium production cells
WO2002066710A1 (en) * 2001-02-23 2002-08-29 Norsk Hydro Asa A material for a dimensionally stable anode for the electrowinning of aluminium

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090136122A1 (en) * 2007-11-27 2009-05-28 Alcoa Inc. Systems and methods for inspecting anodes and smelting management relating to the same
WO2009070477A1 (en) * 2007-11-27 2009-06-04 Alcoa Inc. Systems and methods for inspecting anodes and smelting management relating to the same
US8594417B2 (en) 2007-11-27 2013-11-26 Alcoa Inc. Systems and methods for inspecting anodes and smelting management relating to the same

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